- 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-1-ethanol
- 2-Butoxy-aethanol
- 2-Butoxyethan-1-ol
- 2-Butoxyethanol
- 2-Hydroxyethyl n-butyl ether
- 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 cellosolve
- Butyl glycol
- Butyl icinol
- Butyl monoether glycol
- Butyl oxitol
- Butylcelosolv
- Chimec NR
- Dowanol EB
- EGBE
- Ektasolve EB
- Ektasolve EB solvent
- Ether alcohol
- Ethylene glycol butyl ether
- Ethylene glycol mono-n-butyl ether
- Ethylene glycol monobutyl ether
- Ethylene glycol n-butyl ether
- Gafcol EB
- Glycol butyl ether
- Glycol ether EB
- Glycol ether eb acetate
- Glycol monobutyl ether
- Jeffersol EB
- Minex BDH
- Monobutyl ether of ethylene glycol
- Monobutyl glycol ether
- NSC 60759
- O-Butyl ethylene glycol
- Poly-Solv EB
- UN 2369
- n-Butoxyethanol
- n-Butyl cellosolve
- «beta»-Butoxyethanol
- «beta»-Butoxyethanol
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- 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).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- 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.
- I : Polar retention indices.
- csound,fluid : Speed of sound in fluid (m/s).
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (K).
- Tc : Critical Temperature (K).
- λ : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- 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 |
|---|---|---|---|
| ΔfG° | -242.18 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -451.62 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 16.57 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 56.59 | kJ/mol | NIST |
| log10WS | [-0.42; -0.42] |
|
|
| log10WS | -0.42 | Aq. Sol... | |
| log10WS | -0.42 | Estimat... | |
| logPoct/wat | 0.795 | Crippen Calculated Property | |
| McVol | 107.140 | ml/mol | McGowan Calculated Property |
| 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 | |
| I | [1361.00; 1455.00] |
|
|
| I | 1416.00 | NIST | |
| I | 1403.00 | NIST | |
| I | 1391.00 | NIST | |
| I | 1405.00 | NIST | |
| I | 1389.00 | NIST | |
| I | Outlier 1361.00 | NIST | |
| I | 1393.00 | NIST | |
| I | 1392.00 | NIST | |
| I | 1426.00 | NIST | |
| I | 1391.00 | NIST | |
| I | 1429.70 | NIST | |
| I | Outlier 1447.00 | NIST | |
| I | 1404.00 | NIST | |
| I | 1413.00 | NIST | |
| I | 1395.00 | NIST | |
| I | 1395.00 | NIST | |
| I | 1404.00 | NIST | |
| I | 1379.00 | NIST | |
| I | 1411.00 | NIST | |
| I | 1411.00 | NIST | |
| I | 1405.00 | NIST | |
| I | 1410.00 | NIST | |
| I | 1406.00 | NIST | |
| I | 1406.00 | NIST | |
| I | 1435.00 | NIST | |
| I | 1430.00 | NIST | |
| I | 1399.00 | NIST | |
| I | 1402.00 | NIST | |
| I | Outlier 1455.00 | NIST | |
| I | 1407.00 | NIST | |
| I | 1441.00 | NIST | |
| I | 1371.00 | NIST | |
| I | 1379.00 | NIST | |
| I | 1385.00 | NIST | |
| I | 1397.00 | NIST | |
| I | 1418.00 | NIST | |
| I | 1419.00 | NIST | |
| I | 1402.00 | NIST | |
| I | 1404.00 | NIST | |
| I | 1371.00 | NIST | |
| I | 1433.00 | NIST | |
| I | 1391.00 | NIST | |
| I | 1395.00 | NIST | |
| I | 1408.00 | NIST | |
| I | 1391.00 | NIST | |
| I | 1403.00 | NIST | |
| I | 1406.00 | NIST | |
| I | 1402.00 | NIST | |
| I | 1416.00 | NIST | |
| I | 1405.00 | NIST | |
| I | 1426.00 | NIST | |
| I | 1413.00 | NIST | |
| I | 1411.00 | NIST | |
| I | 1407.00 | NIST | |
| I | 1397.00 | NIST | |
| I | 1371.00 | NIST | |
| Tboil | [442.60; 444.35] | K |
|
| 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; 633.90] | K |
|
| Tc | 633.90 ± 1.00 | K | NIST |
| Tc | 633.90 ± 1.20 | K | NIST |
| Tfus | [196.88; 202.75] | K |
|
| Tfus | 196.88 | K | Aq. Sol... |
| Tfus | 202.75 | K | NIST |
| Vc | 0.408 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [230.19; 282.03] | J/mol×K | [451.28; 612.56] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 230 240 250 260 270 280 450 500 550 600 | ||||
| Cp,gas | 230.19 | J/mol×K | 451.28 | Joback Calculated Property |
| Cp,gas | 239.54 | J/mol×K | 478.16 | Joback Calculated Property |
| Cp,gas | 248.61 | J/mol×K | 505.04 | Joback Calculated Property |
| Cp,gas | 257.39 | J/mol×K | 531.92 | Joback Calculated Property |
| Cp,gas | 265.89 | J/mol×K | 558.80 | Joback Calculated Property |
| Cp,gas | 274.10 | J/mol×K | 585.68 | Joback Calculated Property |
| Cp,gas | 282.03 | J/mol×K | 612.56 | Joback Calculated Property |
| Cp,liquid | [261.70; 293.60] | J/mol×K | [275.15; 339.15] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 260 265 270 275 280 285 290 295 280 300 320 340 | ||||
| Cp,liquid | 261.70 | J/mol×K | 275.15 | Measure... |
| Cp,liquid | 262.60 | J/mol×K | 277.15 | Measure... |
| Cp,liquid | 263.60 | J/mol×K | 279.15 | Measure... |
| Cp,liquid | 264.60 | J/mol×K | 281.15 | Measure... |
| Cp,liquid | 265.60 | J/mol×K | 283.15 | Measure... |
| Cp,liquid | 266.60 | J/mol×K | 285.15 | Measure... |
| Cp,liquid | 267.60 | J/mol×K | 287.15 | Measure... |
| Cp,liquid | 268.50 | J/mol×K | 289.15 | Measure... |
| Cp,liquid | 269.50 | J/mol×K | 291.15 | Measure... |
| Cp,liquid | 270.50 | J/mol×K | 293.15 | Measure... |
| Cp,liquid | 271.50 | J/mol×K | 295.15 | Measure... |
| Cp,liquid | 272.50 | J/mol×K | 297.15 | Measure... |
| Cp,liquid | 273.00 | J/mol×K | 298.15 | Measure... |
| Cp,liquid | 273.10 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 270.60 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 273.30 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 273.50 | J/mol×K | 299.15 | Measure... |
| Cp,liquid | 274.50 | J/mol×K | 301.15 | Measure... |
| Cp,liquid | 275.50 | J/mol×K | 303.15 | Measure... |
| Cp,liquid | 276.50 | J/mol×K | 305.15 | Measure... |
| Cp,liquid | 277.50 | J/mol×K | 307.15 | Measure... |
| Cp,liquid | 278.50 | J/mol×K | 309.15 | Measure... |
| Cp,liquid | 279.50 | J/mol×K | 311.15 | Measure... |
| Cp,liquid | 280.50 | J/mol×K | 313.15 | Measure... |
| Cp,liquid | 281.50 | J/mol×K | 315.15 | Measure... |
| Cp,liquid | 282.50 | J/mol×K | 317.15 | Measure... |
| Cp,liquid | 283.50 | J/mol×K | 319.15 | Measure... |
| Cp,liquid | 284.50 | J/mol×K | 321.15 | Measure... |
| Cp,liquid | 285.50 | J/mol×K | 323.15 | Measure... |
| Cp,liquid | 286.50 | J/mol×K | 325.15 | Measure... |
| Cp,liquid | 287.50 | J/mol×K | 327.15 | Measure... |
| Cp,liquid | 288.50 | J/mol×K | 329.15 | Measure... |
| Cp,liquid | 289.60 | J/mol×K | 331.15 | Measure... |
| Cp,liquid | 290.60 | J/mol×K | 333.15 | Measure... |
| Cp,liquid | 291.60 | J/mol×K | 335.15 | Measure... |
| Cp,liquid | 292.60 | J/mol×K | 337.15 | Measure... |
| Cp,liquid | 293.60 | J/mol×K | 339.15 | Measure... |
| η | [0.0019459; 0.0027820] | Pa×s | [298.15; 313.15] |
|
|
T(K) Dynamic viscosity (Pa×s) 2.00e-3 2.20e-3 2.40e-3 2.60e-3 2.80e-3 300 305 310 | ||||
| η | 0.0027820 | Pa×s | 298.15 | Densiti... |
| η | 0.0027817 | Pa×s | 298.15 | Conduct... |
| η | 0.0024993 | Pa×s | 303.15 | Conduct... |
| η | 0.0022060 | Pa×s | 308.15 | Densiti... |
| η | 0.0022064 | Pa×s | 308.15 | Conduct... |
| η | 0.0019459 | Pa×s | 313.15 | Conduct... |
| ΔfusH | 11.80 | kJ/mol | 199.50 | NIST |
| ΔvapH | [49.50; 52.60] | kJ/mol | [372.50; 389.50] |
|
| ΔvapH | 51.20 | kJ/mol | 372.50 | NIST |
| ΔvapH | 49.50 | kJ/mol | 389.50 | NIST |
| ΔvapH | 52.60 | kJ/mol | 389.50 | NIST |
| Pvap | [28.10; 95.30] | kPa | [406.80; 442.49] |
|
|
T(K) Vapor pressure (kPa) 30 40 50 60 70 80 90 100 410 420 430 440 | ||||
| Pvap | 28.10 | kPa | 406.80 | Vapor-l... |
| Pvap | 34.20 | kPa | 412.10 | Vapor-l... |
| Pvap | 41.30 | kPa | 417.35 | Vapor-l... |
| Pvap | 47.90 | kPa | 421.57 | Vapor-l... |
| Pvap | 53.70 | kPa | 424.90 | Vapor-l... |
| Pvap | 60.50 | kPa | 428.43 | Vapor-l... |
| Pvap | 68.60 | kPa | 432.22 | Vapor-l... |
| Pvap | 76.40 | kPa | 435.52 | Vapor-l... |
| Pvap | 81.20 | kPa | 437.42 | Vapor-l... |
| Pvap | 88.70 | kPa | 440.20 | Vapor-l... |
| Pvap | 93.90 | kPa | 441.30 | Estimat... |
| Pvap | 93.60 | kPa | 441.50 | Estimat... |
| Pvap | 94.10 | kPa | 442.10 | Estimat... |
| Pvap | 95.30 | kPa | 442.49 | Vapor-l... |
| n0 | [1.40701; 1.42260] | [283.15; 323.15] |
|
|
|
T(K) Refractive Index 1.41 1.42 1.42 290 300 310 320 | ||||
| n0 | 1.42260 | 283.15 | Density... | |
| n0 | 1.41960 | 293.15 | Density... | |
| n0 | 1.41710 | 298.15 | Density... | |
| n0 | 1.41570 | 303.15 | Density... | |
| n0 | 1.41500 | 303.15 | Densiti... | |
| n0 | 1.41139 | 313.15 | Density... | |
| n0 | 1.40701 | 323.15 | Density... | |
| ρl | [848.30; 900.64] | kg/m3 | [293.15; 353.15] |
|
|
T(K) Liquid Density (kg/m3) 850 860 870 880 890 900 300 320 340 | ||||
| ρl | 900.64 | kg/m3 | 293.15 | Liquid ... |
| ρl | 900.40 | kg/m3 | 293.15 | Density... |
| ρl | 896.16 | kg/m3 | 298.15 | Experim... |
| ρl | 896.20 | kg/m3 | 298.15 | Density... |
| ρl | 896.17 | kg/m3 | 298.15 | Thermod... |
| ρl | 896.25 | kg/m3 | 298.15 | Excess ... |
| ρl | 896.31 | kg/m3 | 298.15 | Thermod... |
| ρl | 896.46 | kg/m3 | 298.15 | FT-IR s... |
| ρl | 896.31 | kg/m3 | 298.15 | Thermod... |
| ρl | 896.16 | kg/m3 | 298.15 | Electri... |
| ρl | 892.22 | kg/m3 | 303.15 | FT-IR s... |
| ρl | 892.00 | kg/m3 | 303.15 | Density... |
| ρl | 887.80 | kg/m3 | 308.15 | Density... |
| ρl | 887.97 | kg/m3 | 308.15 | FT-IR s... |
| ρl | 883.80 | kg/m3 | 313.15 | Liquid ... |
| ρl | 883.50 | kg/m3 | 313.15 | Density... |
| ρl | 883.70 | kg/m3 | 313.15 | FT-IR s... |
| ρl | 879.42 | kg/m3 | 318.15 | FT-IR s... |
| ρl | 879.20 | kg/m3 | 318.15 | Density... |
| ρl | 874.90 | kg/m3 | 323.15 | Density... |
| ρl | 870.60 | kg/m3 | 328.15 | Density... |
| ρl | 866.20 | kg/m3 | 333.15 | Density... |
| ρl | 861.80 | kg/m3 | 338.15 | Density... |
| ρl | 857.30 | kg/m3 | 343.15 | Density... |
| ρl | 852.80 | kg/m3 | 348.15 | Density... |
| ρl | 848.30 | kg/m3 | 353.15 | Density... |
| csound,fluid | [1242.10; 1304.00] | m/s | [298.15; 318.15] |
|
|
T(K) Speed of sound in fluid (m/s) 1240 1250 1260 1270 1280 1290 1300 1310 300 305 310 315 | ||||
| csound,fluid | 1304.00 | m/s | 298.15 | Densiti... |
| csound,fluid | 1288.50 | m/s | 303.15 | Densiti... |
| csound,fluid | 1275.00 | m/s | 308.15 | Densiti... |
| csound,fluid | 1285.00 | m/s | 308.15 | Densiti... |
| csound,fluid | 1259.00 | m/s | 313.15 | Densiti... |
| csound,fluid | 1242.10 | m/s | 318.15 | Densiti... |
| λ | [0.12; 0.14] | W/m×K | [283.96; 373.84] |
|
|
T(K) Liquid thermal conductivity (W/m×K) 0.12 0.13 0.13 0.13 0.13 0.13 0.14 0.14 300 320 340 360 | ||||
| λ | 0.14 | W/m×K | 283.96 | Thermal... |
| λ | 0.14 | W/m×K | 293.67 | Thermal... |
| λ | 0.14 | W/m×K | 303.56 | Thermal... |
| λ | 0.13 | W/m×K | 314.25 | Thermal... |
| λ | 0.13 | W/m×K | 323.88 | Thermal... |
| λ | 0.13 | W/m×K | 333.98 | Thermal... |
| λ | 0.13 | W/m×K | 344.05 | Thermal... |
| λ | 0.13 | W/m×K | 354.63 | Thermal... |
| λ | 0.13 | W/m×K | 363.59 | Thermal... |
| λ | 0.12 | W/m×K | 373.84 | Thermal... |
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 |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [341.68; 468.10] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| 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 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
| 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 |
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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)
Find more compounds similar to Ethanol, 2-butoxy-.
Mixtures
- Ethanol, 2-butoxy- + 1-Butanol, 3-methyl-
- Ethanol, 2-butoxy- + 2-Pyrrolidinone, 1-methyl-
- 1-Propanol + Ethanol, 2-butoxy-
- Ethanol, 2-butoxy- + Isopropyl Alcohol
- Ethanol, 2-butoxy- + 1-Butanol
- Ethanol, 2-butoxy- + Octane + Water
- n-Hexane + Ethanol, 2-butoxy-
- Ethanol, 2-butoxy- + Heptane
- Ethanol, 2-butoxy- + 1-Hexanol
- Ethanol, 2-butoxy- + 1-Octanol
- Ethanol, 2-butoxy- + 1-Decanol
- Ethanol, 2-butoxy- + Water
- Ethanol, 2-butoxy- + Benzyl alcohol
- Ethanol, 2-butoxy- + Methyl Alcohol
- Ethanol, 2-butoxy- + Ethanol
- Ethanol, 2-butoxy- + Propanoic acid, 2-hydroxy-, ethyl ester
- Ethanol, 2-butoxy- + Phosphonic acid, phenyl-
- Ethanol, 2-butoxy- + Ethanol, 2-(methylamino)-
- Benzene + Ethanol, 2-butoxy-
- Toluene + Ethanol, 2-butoxy-
Find more mixtures with Ethanol, 2-butoxy-.
Sources
- Crippen Method
- 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
- Effect of hydrophilic additives on volumetric and viscosity properties of amino acids in aqueous solutions at T = (283.15 to 333.15) K
- Thermodynamic, transport and excess properties of 2-butoxy ethanol +1-alkanol (C6,C8,C10) at different temperatures
- 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
- 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
- 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
- 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
- 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
- The Yaws Handbook of Vapor Pressure
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