- InChI
- InChI=1S/C8H18O3/c1-2-3-5-10-7-8-11-6-4-9/h9H,2-8H2,1H3
- InChI Key
- OAYXUHPQHDHDDZ-UHFFFAOYSA-N
- Formula
- C8H18O3
- SMILES
- CCCCOCCOCCO
- Molecular Weight1
- 162.23
- CAS
- 112-34-5
- Other Names
-
- 2-(2-Butoxyethoxy)ethanol
- 2-(2-n-Butoxyethoxy)ethanol
- 2-2-Butoxyethoxy;ethanol
- 3,6-Dioxa-1-decanol
- 3,6-Dioxadecanol
- BuCb
- Butadigol
- Butoxydiethylene glycol
- Butoxydiglycol
- Butoxyethoxyethanol
- Butyl Carbitol
- Butyl Oxitol glycol ether
- Butyl di-icinol
- Butyl diglycol
- Butyl digol
- Butyl dioxitol
- Diethylene DB
- Diethylene glycol butyl ester
- Diethylene glycol butyl ether
- Diethylene glycol mono-n-butyl ether
- Diethylene glycol monobutyl ether
- Diethylene glycol n-butyl ether
- Diethylene gylcol monobutyl ether
- Diglycol monobutyl ether
- Dowanol DB
- Dowanol OR
- Ektasolve DB
- Ethanol 2-butoxyethoxy
- Ethanol, 2,2'-oxybis-, monobutyl ether
- Ethylene glycol monobutyl ether
- Glycol ether DB
- Glycol, monobutyl ether
- Jeffersol DB
- NSC 407762
- O-Butyl diethylene glycol
- Poly-Solv DB
- diethylene glycol, n-butyl ether
- n-Butyl carbitol
- 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).
- 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.
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (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
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔfG° | -330.34 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -625.12 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 22.94 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 54.90 | kJ/mol | Joback Calculated Property |
| log10WS | -0.61 | Crippen Calculated Property | |
| logPoct/wat | 0.812 | Crippen Calculated Property | |
| McVol | 141.190 | ml/mol | McGowan Calculated Property |
| Pc | 2790.00 ± 70.00 | kPa | NIST |
| Inp | [1169.00; 1211.00] |
|
|
| Inp | 1193.00 | NIST | |
| Inp | 1192.00 | NIST | |
| Inp | 1188.00 | NIST | |
| Inp | 1196.00 | NIST | |
| Inp | 1194.50 | NIST | |
| Inp | 1189.00 | NIST | |
| Inp | 1198.00 | NIST | |
| Inp | Outlier 1169.00 | NIST | |
| Inp | Outlier 1169.00 | NIST | |
| Inp | 1174.00 | NIST | |
| Inp | 1188.00 | NIST | |
| Inp | 1195.00 | NIST | |
| Inp | 1184.00 | NIST | |
| Inp | 1196.20 | NIST | |
| Inp | 1192.00 | NIST | |
| Inp | Outlier 1211.00 | NIST | |
| Inp | 1186.00 | NIST | |
| Inp | 1186.00 | NIST | |
| Inp | 1188.00 | NIST | |
| I | [1749.00; 1827.00] |
|
|
| I | 1760.00 | NIST | |
| I | 1749.00 | NIST | |
| I | 1827.00 | NIST | |
| I | 1796.00 | NIST | |
| I | 1786.00 | NIST | |
| I | 1786.00 | NIST | |
| I | 1796.00 | NIST | |
| I | 1797.00 | NIST | |
| I | 1823.00 | NIST | |
| I | 1823.00 | NIST | |
| I | 1791.00 | NIST | |
| I | 1781.00 | NIST | |
| I | 1797.00 | NIST | |
| I | 1823.00 | NIST | |
| I | 1760.00 | NIST | |
| Tboil | [504.20; 504.35] | K |
|
| Tboil | 504.20 | K | NIST |
| Tboil | 504.35 ± 0.50 | K | NIST |
| Tc | 692.30 ± 1.50 | K | NIST |
| Tfus | 285.20 | K | Joback Calculated Property |
| Vc | 0.538 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [339.16; 401.64] | J/mol×K | [519.46; 679.35] |
|
| Cp,gas | 339.16 | J/mol×K | 519.46 | Joback Calculated Property |
| Cp,gas | 350.45 | J/mol×K | 546.11 | Joback Calculated Property |
| Cp,gas | 361.39 | J/mol×K | 572.76 | Joback Calculated Property |
| Cp,gas | 371.99 | J/mol×K | 599.41 | Joback Calculated Property |
| Cp,gas | 382.23 | J/mol×K | 626.06 | Joback Calculated Property |
| Cp,gas | 392.11 | J/mol×K | 652.70 | Joback Calculated Property |
| Cp,gas | 401.64 | J/mol×K | 679.35 | Joback Calculated Property |
| Cp,liquid | [351.20; 380.10] | J/mol×K | [275.15; 339.15] |
|
| Cp,liquid | 351.20 | J/mol×K | 275.15 | Measure... |
| Cp,liquid | 351.90 | J/mol×K | 277.15 | Measure... |
| Cp,liquid | 352.70 | J/mol×K | 279.15 | Measure... |
| Cp,liquid | 353.40 | J/mol×K | 281.15 | Measure... |
| Cp,liquid | 354.20 | J/mol×K | 283.15 | Measure... |
| Cp,liquid | 354.90 | J/mol×K | 285.15 | Measure... |
| Cp,liquid | 355.70 | J/mol×K | 287.15 | Measure... |
| Cp,liquid | 356.50 | J/mol×K | 289.15 | Measure... |
| Cp,liquid | 357.30 | J/mol×K | 291.15 | Measure... |
| Cp,liquid | 358.10 | J/mol×K | 293.15 | Measure... |
| Cp,liquid | 359.00 | J/mol×K | 295.15 | Measure... |
| Cp,liquid | 359.80 | J/mol×K | 297.15 | Measure... |
| Cp,liquid | 360.20 | J/mol×K | 298.15 | Measure... |
| Cp,liquid | 354.89 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 360.60 | J/mol×K | 299.15 | Measure... |
| Cp,liquid | 361.50 | J/mol×K | 301.15 | Measure... |
| Cp,liquid | 362.40 | J/mol×K | 303.15 | Measure... |
| Cp,liquid | 363.30 | J/mol×K | 305.15 | Measure... |
| Cp,liquid | 364.20 | J/mol×K | 307.15 | Measure... |
| Cp,liquid | 365.10 | J/mol×K | 309.15 | Measure... |
| Cp,liquid | 366.00 | J/mol×K | 311.15 | Measure... |
| Cp,liquid | 366.90 | J/mol×K | 313.15 | Measure... |
| Cp,liquid | 367.90 | J/mol×K | 315.15 | Measure... |
| Cp,liquid | 368.80 | J/mol×K | 317.15 | Measure... |
| Cp,liquid | 369.80 | J/mol×K | 319.15 | Measure... |
| Cp,liquid | 370.80 | J/mol×K | 321.15 | Measure... |
| Cp,liquid | 371.80 | J/mol×K | 323.15 | Measure... |
| Cp,liquid | 372.80 | J/mol×K | 325.15 | Measure... |
| Cp,liquid | 373.80 | J/mol×K | 327.15 | Measure... |
| Cp,liquid | 374.80 | J/mol×K | 329.15 | Measure... |
| Cp,liquid | 375.80 | J/mol×K | 331.15 | Measure... |
| Cp,liquid | 376.90 | J/mol×K | 333.15 | Measure... |
| Cp,liquid | 377.90 | J/mol×K | 335.15 | Measure... |
| Cp,liquid | 379.00 | J/mol×K | 337.15 | Measure... |
| Cp,liquid | 380.10 | J/mol×K | 339.15 | Measure... |
| η | [0.0020000; 0.0058400] | Pa×s | [293.15; 333.15] |
|
| η | 0.0058400 | Pa×s | 293.15 | Excess ... |
| η | 0.0042300 | Pa×s | 303.15 | Excess ... |
| η | 0.0032200 | Pa×s | 313.15 | Excess ... |
| η | 0.0025100 | Pa×s | 323.15 | Excess ... |
| η | 0.0020000 | Pa×s | 333.15 | Excess ... |
| ΔvapH | 55.70 | kJ/mol | 460.00 | NIST |
| n0 | [1.41940; 1.43470] | [283.15; 323.15] |
|
|
| n0 | 1.43470 | 283.15 | Density... | |
| n0 | 1.43120 | 293.15 | Density... | |
| n0 | 1.42998 | 298.15 | Excess ... | |
| n0 | 1.42950 | 298.15 | Density... | |
| n0 | 1.42805 | 303.15 | Density... | |
| n0 | 1.42400 | 313.15 | Density... | |
| n0 | 1.41940 | 323.15 | Density... | |
| ρl | [918.50; 952.90] | kg/m3 | [293.15; 333.15] |
|
| ρl | 952.90 | kg/m3 | 293.15 | Density... |
| ρl | 952.29 | kg/m3 | 293.15 | FT-IR s... |
| ρl | 948.10 | kg/m3 | 298.15 | FT-IR s... |
| ρl | 947.98 | kg/m3 | 298.15 | Speeds ... |
| ρl | 943.91 | kg/m3 | 303.15 | FT-IR s... |
| ρl | 943.50 | kg/m3 | 303.15 | Density... |
| ρl | 939.70 | kg/m3 | 308.15 | FT-IR s... |
| ρl | 935.50 | kg/m3 | 313.15 | FT-IR s... |
| ρl | 935.70 | kg/m3 | 313.15 | Density... |
| ρl | 926.60 | kg/m3 | 323.15 | Density... |
| ρl | 918.50 | kg/m3 | 333.15 | Density... |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 283.15 | 100.00 | 960.4 |
| 283.15 | 1000.00 | 961.3 |
| 283.15 | 3000.00 | 962.6 |
| 283.15 | 5000.00 | 963.4 |
| 283.15 | 10000.00 | 966.5 |
| 283.15 | 15000.00 | 969.4 |
| 283.15 | 20000.00 | 971.9 |
| 283.15 | 25000.00 | 974.5 |
| 283.15 | 30000.00 | 977.1 |
| 283.15 | 35000.00 | 979.1 |
| 283.15 | 40000.00 | 981.4 |
| 283.15 | 50000.00 | 986.9 |
| 283.15 | 60000.00 | 990.4 |
| 293.15 | 100.00 | 952.4 |
| 293.15 | 1000.00 | 952.9 |
| 293.15 | 3000.00 | 954.3 |
| 293.15 | 5000.00 | 955.2 |
| 293.15 | 10000.00 | 958.4 |
| 293.15 | 15000.00 | 961.2 |
| 293.15 | 20000.00 | 964.0 |
| 293.15 | 25000.00 | 966.9 |
| 293.15 | 30000.00 | 969.6 |
| 293.15 | 35000.00 | 972.0 |
| 293.15 | 40000.00 | 974.4 |
| 293.15 | 50000.00 | 979.7 |
| 293.15 | 60000.00 | 983.9 |
| 303.15 | 100.00 | 943.8 |
| 303.15 | 1000.00 | 944.2 |
| 303.15 | 3000.00 | 946.0 |
| 303.15 | 5000.00 | 947.0 |
| 303.15 | 10000.00 | 950.3 |
| 303.15 | 15000.00 | 953.0 |
| 303.15 | 20000.00 | 956.0 |
| 303.15 | 25000.00 | 959.1 |
| 303.15 | 30000.00 | 962.0 |
| 303.15 | 35000.00 | 964.7 |
| 303.15 | 40000.00 | 967.1 |
| 303.15 | 50000.00 | 972.2 |
| 303.15 | 60000.00 | 977.1 |
| 313.15 | 100.00 | 935.5 |
| 313.15 | 1000.00 | 935.9 |
| 313.15 | 3000.00 | 937.2 |
| 313.15 | 5000.00 | 938.8 |
| 313.15 | 10000.00 | 942.0 |
| 313.15 | 15000.00 | 945.2 |
| 313.15 | 20000.00 | 948.4 |
| 313.15 | 25000.00 | 951.2 |
| 313.15 | 30000.00 | 953.8 |
| 313.15 | 35000.00 | 956.9 |
| 313.15 | 40000.00 | 959.7 |
| 313.15 | 50000.00 | 965.0 |
| 313.15 | 60000.00 | 969.7 |
| 323.15 | 100.00 | 927.0 |
| 323.15 | 1000.00 | 927.3 |
| 323.15 | 3000.00 | 928.8 |
| 323.15 | 5000.00 | 930.3 |
| 323.15 | 10000.00 | 933.8 |
| 323.15 | 15000.00 | 937.2 |
| 323.15 | 20000.00 | 940.4 |
| 323.15 | 25000.00 | 943.5 |
| 323.15 | 30000.00 | 946.4 |
| 323.15 | 35000.00 | 949.5 |
| 323.15 | 40000.00 | 952.5 |
| 323.15 | 50000.00 | 958.2 |
| 323.15 | 60000.00 | 963.4 |
| 333.15 | 100.00 | 917.8 |
| 333.15 | 1000.00 | 918.7 |
| 333.15 | 3000.00 | 920.7 |
| 333.15 | 5000.00 | 922.2 |
| 333.15 | 10000.00 | 925.7 |
| 333.15 | 15000.00 | 929.2 |
| 333.15 | 20000.00 | 932.5 |
| 333.15 | 25000.00 | 935.5 |
| 333.15 | 30000.00 | 939.0 |
| 333.15 | 35000.00 | 942.0 |
| 333.15 | 40000.00 | 945.2 |
| 333.15 | 50000.00 | 950.6 |
| 333.15 | 60000.00 | 956.0 |
| 343.15 | 100.00 | 909.1 |
| 343.15 | 1000.00 | 910.5 |
| 343.15 | 3000.00 | 912.35 |
| 343.15 | 5000.00 | 913.6 |
| 343.15 | 10000.00 | 917.6 |
| 343.15 | 15000.00 | 921.3 |
| 343.15 | 20000.00 | 924.7 |
| 343.15 | 25000.00 | 928.1 |
| 343.15 | 30000.00 | 931.3 |
| 343.15 | 35000.00 | 934.4 |
| 343.15 | 40000.00 | 937.3 |
| 343.15 | 50000.00 | 943.2 |
| 343.15 | 60000.00 | 948.8 |
| 353.15 | 100.00 | 901.1 |
| 353.15 | 1000.00 | 902.1 |
| 353.15 | 3000.00 | 903.9 |
| 353.15 | 5000.00 | 905.3 |
| 353.15 | 10000.00 | 909.3 |
| 353.15 | 15000.00 | 913.1 |
| 353.15 | 20000.00 | 916.8 |
| 353.15 | 25000.00 | 920.3 |
| 353.15 | 30000.00 | 923.7 |
| 353.15 | 35000.00 | 927.1 |
| 353.15 | 40000.00 | 930.3 |
| 353.15 | 50000.00 | 936.3 |
| 353.15 | 60000.00 | 942.2 |
| 363.15 | 100.00 | 892.6 |
| 363.15 | 1000.00 | 893.2 |
| 363.15 | 3000.00 | 894.9 |
| 363.15 | 5000.00 | 896.7 |
| 363.15 | 10000.00 | 900.4 |
| 363.15 | 15000.00 | 904.8 |
| 363.15 | 20000.00 | 908.5 |
| 363.15 | 25000.00 | 912.1 |
| 363.15 | 30000.00 | 915.7 |
| 363.15 | 35000.00 | 919.2 |
| 363.15 | 40000.00 | 922.7 |
| 363.15 | 50000.00 | 929.1 |
| 363.15 | 60000.00 | 935.2 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 283.15 | 100.00 | 960.5 |
| 283.15 | 1000.00 | 961.0 |
| 283.15 | 2500.00 | 961.9 |
| 283.15 | 5000.00 | 963.4 |
| 283.15 | 7500.00 | 964.9 |
| 283.15 | 10000.00 | 966.3 |
| 283.15 | 15000.00 | 969.1 |
| 283.15 | 20000.00 | 971.8 |
| 283.15 | 25000.00 | 974.4 |
| 293.15 | 100.00 | 952.2 |
| 293.15 | 1000.00 | 952.7 |
| 293.15 | 2500.00 | 953.7 |
| 293.15 | 5000.00 | 955.2 |
| 293.15 | 7500.00 | 956.7 |
| 293.15 | 10000.00 | 958.2 |
| 293.15 | 15000.00 | 961.1 |
| 293.15 | 20000.00 | 963.9 |
| 293.15 | 25000.00 | 966.7 |
| 303.15 | 100.00 | 943.8 |
| 303.15 | 1000.00 | 944.3 |
| 303.15 | 2500.00 | 945.3 |
| 303.15 | 5000.00 | 946.9 |
| 303.15 | 7500.00 | 948.5 |
| 303.15 | 10000.00 | 950.1 |
| 303.15 | 15000.00 | 953.1 |
| 303.15 | 20000.00 | 956.1 |
| 303.15 | 25000.00 | 959.0 |
| 313.15 | 100.00 | 935.3 |
| 313.15 | 1000.00 | 935.9 |
| 313.15 | 2500.00 | 936.9 |
| 313.15 | 5000.00 | 938.6 |
| 313.15 | 7500.00 | 940.3 |
| 313.15 | 10000.00 | 941.9 |
| 313.15 | 15000.00 | 945.1 |
| 313.15 | 20000.00 | 948.2 |
| 313.15 | 25000.00 | 951.2 |
| 323.15 | 100.00 | 926.6 |
| 323.15 | 1000.00 | 927.2 |
| 323.15 | 2500.00 | 928.3 |
| 323.15 | 5000.00 | 930.1 |
| 323.15 | 7500.00 | 931.8 |
| 323.15 | 10000.00 | 933.5 |
| 323.15 | 15000.00 | 936.9 |
| 323.15 | 20000.00 | 940.1 |
| 323.15 | 25000.00 | 943.2 |
| 333.15 | 100.00 | 917.8 |
| 333.15 | 1000.00 | 918.5 |
| 333.15 | 2500.00 | 919.7 |
| 333.15 | 5000.00 | 921.6 |
| 333.15 | 7500.00 | 923.4 |
| 333.15 | 10000.00 | 925.2 |
| 333.15 | 15000.00 | 928.7 |
| 333.15 | 20000.00 | 932.0 |
| 333.15 | 25000.00 | 935.2 |
| 343.15 | 100.00 | 909.7 |
| 343.15 | 1000.00 | 910.4 |
| 343.15 | 2500.00 | 911.6 |
| 343.15 | 5000.00 | 913.6 |
| 343.15 | 7500.00 | 915.5 |
| 343.15 | 10000.00 | 917.4 |
| 343.15 | 15000.00 | 921.1 |
| 343.15 | 20000.00 | 924.6 |
| 343.15 | 25000.00 | 928.0 |
| 353.15 | 100.00 | 900.9 |
| 353.15 | 1000.00 | 901.7 |
| 353.15 | 2500.00 | 903.0 |
| 353.15 | 5000.00 | 905.0 |
| 353.15 | 7500.00 | 907.1 |
| 353.15 | 10000.00 | 909.1 |
| 353.15 | 15000.00 | 912.9 |
| 353.15 | 20000.00 | 916.6 |
| 353.15 | 25000.00 | 920.1 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [383.54; 533.16] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.53016e+01 | |||
| Coefficient B | -4.46698e+03 | |||
| Coefficient C | -8.60200e+01 | |||
| Temperature range, min. | 383.54 | |||
| Temperature range, max. | 533.16 | |||
| Pvap | 1.33 | kPa | 383.54 | Calculated Property |
| Pvap | 2.95 | kPa | 400.16 | Calculated Property |
| Pvap | 6.03 | kPa | 416.79 | Calculated Property |
| Pvap | 11.51 | kPa | 433.41 | Calculated Property |
| Pvap | 20.70 | kPa | 450.04 | Calculated Property |
| Pvap | 35.38 | kPa | 466.66 | Calculated Property |
| Pvap | 57.82 | kPa | 483.29 | Calculated Property |
| Pvap | 90.82 | kPa | 499.91 | Calculated Property |
| Pvap | 137.78 | kPa | 516.54 | Calculated Property |
| Pvap | 202.64 | kPa | 533.16 | 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-(2-butoxyethoxy)-.
Mixtures
- Propylamine + Ethanol, 2-(2-butoxyethoxy)-
- Propane, 1,2-dichloro- + Ethanol, 2-(2-butoxyethoxy)-
- 1-Hexanol + Ethanol, 2-(2-butoxyethoxy)-
- 1-Octanol + Ethanol, 2-(2-butoxyethoxy)-
- 1-Decanol + Ethanol, 2-(2-butoxyethoxy)-
- Monoethanolamine + Ethanol, 2-(2-butoxyethoxy)-
- Diethanolamine + Ethanol, 2-(2-butoxyethoxy)-
- Ethanol, 2-(2-butoxyethoxy)- + Triethanolamine
- Ethanol, 2-(2-butoxyethoxy)- + Water
- Ethanol, 2-(2-butoxyethoxy)- + Dibenzothiophene
- Nitrogen + Ethanol, 2-(2-butoxyethoxy)-
- Decane + Ethanol, 2-(2-butoxyethoxy)- + Water
- sodium chloride + Ethanol, 2-(2-butoxyethoxy)- + Water
Sources
- Crippen Method
- Crippen Method
- Speeds of Sound and Isentropic Compressibilities of n-Alkoxyethanols and Polyethers with Propylamine at 298.15K
- Excess molar volumes and excess molar enthalpies of the binary mixtures of 1,2-dichloropropane with di- and triethylene glycol mono-alkyl ethers at T=298.15K
- FT-IR studies and excess thermodynamic properties of binary liquid mixtures 2-(2-butoxyethoxy) ethanol with 1-hexanol, 1-octanol and 1-decanol at different temperatures
- Solubility of dibenzothiophene in nine organic solvents: Experimental measurement and thermodynamic modelling
- 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
- Liquid-liquid equilibria for the ternary system water + decane + diethylene glycol monobutyl ether at 20 C, 30 C, and 40 C
- PpT Measurements and EoS Predictions of Glycol Ethers from (283.15 to 353.15) K at Pressures up to 25 MPa
- Phase Behavior and Spectroscopic Properties for Ternary Systems Water + Sodium Chloride + Diethylene Glycol Monobutyl Ether at 303.15 K and Atmospheric Pressure
- Density and Viscosity for Binary Mixtures of Diethylene Glycol Monobutyl Ether with Monoethanolamine, Diethanolamine, and Triethanolamine from (293.15 to 333.15) K
- Isothermal Vapor-Liquid Equilibria of Binary Mixtures of Nitrogen with Dimethyl Sulfoxide, N-Methyl-2-pyrrolidone, and Diethylene Glycol Monobutyl Ether at Elevated Pressures
- Excess Molar Volume and Viscosity Deviation for the Binary Mixture of Diethylene Glycol Monobutyl Ether + Water from (293.15 to 333.15) K at Atmospheric Pressure
- 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
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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