- InChI
- InChI=1S/C6H14O3/c1-2-8-5-6-9-4-3-7/h7H,2-6H2,1H3
- InChI Key
- XXJWXESWEXIICW-UHFFFAOYSA-N
- Formula
- C6H14O3
- SMILES
- CCOCCOCCO
- Molecular Weight1
- 134.17
- CAS
- 111-90-0
- Other Names
-
- (Ethoxyethoxy)ethanol
- 1-Hydroxy-3,6-dioxaoctane
- 2-(2'-ethoxyethoxy)ethanol
- 2-(2-Ethoxyethoxy)ethanol
- 2-(Ethoxyethoxy)ethanol
- 2-(«beta»-Ethoxyethoxy)ethanol
- 2-(«beta»-Ethoxyethoxy)ethanol diglycol
- 2-(«beta»-Ethoxyethoxy)ethanol
- 2-(«beta»-Ethoxyethoxy)ethanol diglycol
- 2-2-Ethoxyethoxy;ethanol
- 3,6-Dioxa-1-octanol
- 3,6-Dioxa-1-oktanol
- 3,6-Dioxaoctan-1-ol
- 3-oxa-1,5-pentanediol, ethyl ether
- APV
- Carbitol
- Carbitol cellosolve
- Carbitol low gravity
- Carbitol solvent
- DEGEE
- DEGMEE
- Diethoxol
- Diethylene Glycol ethyl ether
- Diethylene glycol monoethyl ether
- Diethylene glycol monomethyl ether
- Diglycol
- Diglycol monoethyl ether
- Dioxitol
- Dioxitol-low gravity
- Dowanol
- Dowanol 17
- Dowanol DE
- Eastman DE
- Ehanol, 2,2'-oxybis-, monoethyl ether
- Ektasolve DE
- Ektasolve DE, DE-HG
- Ethanol, 2,2'-oxybis-, monoethyl ether
- Ethoxy diglycol
- Ethyl Di-Icinol
- Ethyl carbitol
- Ethyl diethylene glycol
- Ethyl digol
- Ethyldiglycol
- Ethylene diglycol monoethyl ether
- Karbitol
- Losungsmittel apv
- Monoethyl ether of diethylene glycol
- O-Ethyldigol
- Poly-Solv
- Poly-Solv DE
- Poly-solv DE ethanol, 2,2'-oxybis-, monoethyl ether
- Solvent APV Spec
- Solvolsol
- Transcutol
- Transcutol P
- diethylene glycol, ethyl ether
- diethylene glycol, monoethyl ether
- ethyldiethylene glycol
- 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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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔfG° | -347.18 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -583.84 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 17.76 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 50.45 | kJ/mol | Joback Calculated Property |
| log10WS | 0.23 | Crippen Calculated Property | |
| logPoct/wat | 0.032 | Crippen Calculated Property | |
| McVol | 113.010 | ml/mol | McGowan Calculated Property |
| Pc | 3167.00 ± 26.00 | kPa | NIST |
| Inp | [951.00; 1011.00] |
|
|
| Inp | 982.90 | NIST | |
| Inp | Outlier 951.00 | NIST | |
| Inp | 985.00 | NIST | |
| Inp | 985.00 | NIST | |
| Inp | 1006.00 | NIST | |
| Inp | 1001.00 | NIST | |
| Inp | 1003.00 | NIST | |
| Inp | 1007.00 | NIST | |
| Inp | 1009.10 | NIST | |
| Inp | 1011.00 | NIST | |
| Inp | 999.00 | NIST | |
| Inp | 976.00 | NIST | |
| Inp | 1007.10 | NIST | |
| Inp | 986.00 | NIST | |
| Inp | 979.00 | NIST | |
| Inp | 982.90 | NIST | |
| Inp | 976.00 | NIST | |
| Inp | 1006.00 | NIST | |
| I | [1577.00; 1636.00] |
|
|
| I | 1589.00 | NIST | |
| I | 1577.00 | NIST | |
| I | 1579.00 | NIST | |
| I | 1619.00 | NIST | |
| I | 1615.00 | NIST | |
| I | 1622.00 | NIST | |
| I | 1636.00 | NIST | |
| I | 1583.00 | NIST | |
| I | 1628.00 | NIST | |
| I | 1619.00 | NIST | |
| I | 1589.00 | NIST | |
| Tboil | [468.00; 475.20] | K |
|
| Tboil | 475.20 | K | NIST |
| Tboil | 468.00 ± 2.00 | K | NIST |
| Tc | 670.00 ± 4.00 | K | NIST |
| Tfus | 262.66 | K | Joback Calculated Property |
| Vc | 0.426 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [252.66; 304.54] | J/mol×K | [473.70; 635.03] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 250 260 270 280 290 300 500 550 600 | ||||
| Cp,gas | 252.66 | J/mol×K | 473.70 | Joback Calculated Property |
| Cp,gas | 261.94 | J/mol×K | 500.59 | Joback Calculated Property |
| Cp,gas | 270.97 | J/mol×K | 527.48 | Joback Calculated Property |
| Cp,gas | 279.75 | J/mol×K | 554.37 | Joback Calculated Property |
| Cp,gas | 288.27 | J/mol×K | 581.26 | Joback Calculated Property |
| Cp,gas | 296.54 | J/mol×K | 608.15 | Joback Calculated Property |
| Cp,gas | 304.54 | J/mol×K | 635.03 | Joback Calculated Property |
| Cp,liquid | [296.50; 316.10] | J/mol×K | [275.15; 339.15] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 295 300 305 310 315 280 300 320 340 | ||||
| Cp,liquid | 296.50 | J/mol×K | 275.15 | Measure... |
| Cp,liquid | 296.80 | J/mol×K | 277.15 | Measure... |
| Cp,liquid | 297.20 | J/mol×K | 279.15 | Measure... |
| Cp,liquid | 297.60 | J/mol×K | 281.15 | Measure... |
| Cp,liquid | 298.00 | J/mol×K | 283.15 | Measure... |
| Cp,liquid | 298.50 | J/mol×K | 285.15 | Measure... |
| Cp,liquid | 298.90 | J/mol×K | 287.15 | Measure... |
| Cp,liquid | 299.40 | J/mol×K | 289.15 | Measure... |
| Cp,liquid | 299.90 | J/mol×K | 291.15 | Measure... |
| Cp,liquid | 300.40 | J/mol×K | 293.15 | Measure... |
| Cp,liquid | 300.90 | J/mol×K | 295.15 | Measure... |
| Cp,liquid | 301.40 | J/mol×K | 297.15 | Measure... |
| Cp,liquid | 301.70 | J/mol×K | 298.15 | Measure... |
| Cp,liquid | 301.90 | J/mol×K | 299.15 | Measure... |
| Cp,liquid | 302.50 | J/mol×K | 301.15 | Measure... |
| Cp,liquid | 303.10 | J/mol×K | 303.15 | Measure... |
| Cp,liquid | 303.70 | J/mol×K | 305.15 | Measure... |
| Cp,liquid | 304.30 | J/mol×K | 307.15 | Measure... |
| Cp,liquid | 304.90 | J/mol×K | 309.15 | Measure... |
| Cp,liquid | 305.50 | J/mol×K | 311.15 | Measure... |
| Cp,liquid | 306.20 | J/mol×K | 313.15 | Measure... |
| Cp,liquid | 306.90 | J/mol×K | 315.15 | Measure... |
| Cp,liquid | 307.50 | J/mol×K | 317.15 | Measure... |
| Cp,liquid | 308.20 | J/mol×K | 319.15 | Measure... |
| Cp,liquid | 309.00 | J/mol×K | 321.15 | Measure... |
| Cp,liquid | 309.70 | J/mol×K | 323.15 | Measure... |
| Cp,liquid | 310.40 | J/mol×K | 325.15 | Measure... |
| Cp,liquid | 311.20 | J/mol×K | 327.15 | Measure... |
| Cp,liquid | 312.00 | J/mol×K | 329.15 | Measure... |
| Cp,liquid | 312.80 | J/mol×K | 331.15 | Measure... |
| Cp,liquid | 313.60 | J/mol×K | 333.15 | Measure... |
| Cp,liquid | 314.40 | J/mol×K | 335.15 | Measure... |
| Cp,liquid | 315.20 | J/mol×K | 337.15 | Measure... |
| Cp,liquid | 316.10 | J/mol×K | 339.15 | Measure... |
| η | [0.0035310; 0.0044640] | Pa×s | [293.15; 303.15] |
|
| η | 0.0044640 | Pa×s | 293.15 | Viscosi... |
| η | 0.0039760 | Pa×s | 298.15 | Viscosi... |
| η | 0.0035310 | Pa×s | 303.15 | Viscosi... |
| ΔvapH | 52.10 | kJ/mol | 396.50 | NIST |
| n0 | [1.42500; 1.42530] | [298.15; 298.15] |
|
|
| n0 | 1.42530 | 298.15 | Density... | |
| n0 | 1.42500 | 298.15 | Thermod... | |
| n0 | 1.42530 | 298.15 | Volumet... | |
| ρl | [916.80; 997.10] | kg/m3 | [283.15; 373.15] |
|
|
T(K) Liquid Density (kg/m3) 920 940 960 980 1000 300 320 340 360 | ||||
| ρl | 997.10 | kg/m3 | 283.15 | Thermop... |
| ρl | 992.17 | kg/m3 | 288.15 | Density... |
| ρl | 993.90 | kg/m3 | 288.15 | Thermop... |
| ρl | 992.60 | kg/m3 | 288.15 | Thermop... |
| ρl | 988.20 | kg/m3 | 293.15 | Thermop... |
| ρl | 989.40 | kg/m3 | 293.15 | Thermop... |
| ρl | 984.90 | kg/m3 | 298.15 | Thermop... |
| ρl | 983.70 | kg/m3 | 298.15 | Thermop... |
| ρl | 983.11 | kg/m3 | 298.15 | Density... |
| ρl | 983.08 | kg/m3 | 298.15 | Density... |
| ρl | 983.84 | kg/m3 | 298.15 | Speeds ... |
| ρl | 979.30 | kg/m3 | 303.15 | Thermop... |
| ρl | 980.40 | kg/m3 | 303.15 | Thermop... |
| ρl | 974.80 | kg/m3 | 308.15 | Thermop... |
| ρl | 974.18 | kg/m3 | 308.15 | Density... |
| ρl | 976.00 | kg/m3 | 308.15 | Thermop... |
| ρl | 974.27 | kg/m3 | 308.15 | Density... |
| ρl | 974.67 | kg/m3 | 308.50 | Excess ... |
| ρl | 970.30 | kg/m3 | 313.15 | Thermop... |
| ρl | 971.50 | kg/m3 | 313.15 | Thermop... |
| ρl | 967.00 | kg/m3 | 318.15 | Thermop... |
| ρl | 965.33 | kg/m3 | 318.15 | Density... |
| ρl | 965.33 | kg/m3 | 318.15 | Density... |
| ρl | 962.50 | kg/m3 | 323.15 | Thermop... |
| ρl | 961.30 | kg/m3 | 323.15 | Thermop... |
| ρl | 958.10 | kg/m3 | 328.15 | Thermop... |
| ρl | 953.50 | kg/m3 | 333.15 | Thermop... |
| ρl | 952.20 | kg/m3 | 333.15 | Thermop... |
| ρl | 949.00 | kg/m3 | 338.15 | Thermop... |
| ρl | 944.40 | kg/m3 | 343.15 | Thermop... |
| ρl | 943.10 | kg/m3 | 343.15 | Thermop... |
| ρl | 939.90 | kg/m3 | 348.15 | Thermop... |
| ρl | 935.30 | kg/m3 | 353.15 | Thermop... |
| ρl | 930.70 | kg/m3 | 358.15 | Thermop... |
| ρl | 926.10 | kg/m3 | 363.15 | Thermop... |
| ρl | 921.40 | kg/m3 | 368.15 | Thermop... |
| ρl | 916.80 | kg/m3 | 373.15 | Thermop... |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 283.15 | 100.00 | 997.7 |
| 283.15 | 1000.00 | 998.2 |
| 283.15 | 2500.00 | 999.1 |
| 283.15 | 5000.00 | 1000.6 |
| 283.15 | 7500.00 | 1002.0 |
| 283.15 | 10000.00 | 1003.4 |
| 283.15 | 15000.00 | 1006.1 |
| 283.15 | 20000.00 | 1008.8 |
| 283.15 | 25000.00 | 1011.3 |
| 293.15 | 100.00 | 988.4 |
| 293.15 | 1000.00 | 988.9 |
| 293.15 | 2500.00 | 989.8 |
| 293.15 | 5000.00 | 991.3 |
| 293.15 | 7500.00 | 992.8 |
| 293.15 | 10000.00 | 994.3 |
| 293.15 | 15000.00 | 997.2 |
| 293.15 | 20000.00 | 999.9 |
| 293.15 | 25000.00 | 1002.6 |
| 303.15 | 100.00 | 979.5 |
| 303.15 | 1000.00 | 980.1 |
| 303.15 | 2500.00 | 981.1 |
| 303.15 | 5000.00 | 982.6 |
| 303.15 | 7500.00 | 984.2 |
| 303.15 | 10000.00 | 985.8 |
| 303.15 | 15000.00 | 988.8 |
| 303.15 | 20000.00 | 991.7 |
| 303.15 | 25000.00 | 994.6 |
| 313.15 | 100.00 | 970.6 |
| 313.15 | 1000.00 | 971.2 |
| 313.15 | 2500.00 | 972.2 |
| 313.15 | 5000.00 | 973.9 |
| 313.15 | 7500.00 | 975.5 |
| 313.15 | 10000.00 | 977.1 |
| 313.15 | 15000.00 | 980.3 |
| 313.15 | 20000.00 | 983.4 |
| 313.15 | 25000.00 | 986.3 |
| 323.15 | 100.00 | 961.5 |
| 323.15 | 1000.00 | 962.1 |
| 323.15 | 2500.00 | 963.2 |
| 323.15 | 5000.00 | 965.0 |
| 323.15 | 7500.00 | 966.8 |
| 323.15 | 10000.00 | 968.5 |
| 323.15 | 15000.00 | 971.9 |
| 323.15 | 20000.00 | 975.1 |
| 323.15 | 25000.00 | 978.2 |
| 333.15 | 100.00 | 952.4 |
| 333.15 | 1000.00 | 953.1 |
| 333.15 | 2500.00 | 954.3 |
| 333.15 | 5000.00 | 956.1 |
| 333.15 | 7500.00 | 958.0 |
| 333.15 | 10000.00 | 959.7 |
| 333.15 | 15000.00 | 963.2 |
| 333.15 | 20000.00 | 966.5 |
| 333.15 | 25000.00 | 969.8 |
| 343.15 | 100.00 | 943.4 |
| 343.15 | 1000.00 | 944.1 |
| 343.15 | 2500.00 | 945.3 |
| 343.15 | 5000.00 | 947.3 |
| 343.15 | 7500.00 | 949.2 |
| 343.15 | 10000.00 | 951.1 |
| 343.15 | 15000.00 | 954.8 |
| 343.15 | 20000.00 | 958.3 |
| 343.15 | 25000.00 | 961.6 |
| 353.15 | 100.00 | 934.1 |
| 353.15 | 1000.00 | 934.9 |
| 353.15 | 2500.00 | 936.1 |
| 353.15 | 5000.00 | 938.2 |
| 353.15 | 7500.00 | 940.2 |
| 353.15 | 10000.00 | 942.2 |
| 353.15 | 15000.00 | 946.0 |
| 353.15 | 20000.00 | 949.7 |
| 353.15 | 25000.00 | 953.2 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [357.45; 502.40] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.63980e+01 | |||
| Coefficient B | -5.15308e+03 | |||
| Coefficient C | -3.75940e+01 | |||
| Temperature range, min. | 357.45 | |||
| Temperature range, max. | 502.40 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 400 450 500 | ||||
| Pvap | 1.33 | kPa | 357.45 | Calculated Property |
| Pvap | 2.89 | kPa | 373.56 | Calculated Property |
| Pvap | 5.82 | kPa | 389.66 | Calculated Property |
| Pvap | 11.04 | kPa | 405.77 | Calculated Property |
| Pvap | 19.85 | kPa | 421.87 | Calculated Property |
| Pvap | 34.04 | kPa | 437.98 | Calculated Property |
| Pvap | 56.00 | kPa | 454.08 | Calculated Property |
| Pvap | 88.76 | kPa | 470.19 | Calculated Property |
| Pvap | 136.12 | kPa | 486.29 | Calculated Property |
| Pvap | 202.65 | kPa | 502.40 | Calculated Property |
Similar Compounds
![Ethanol, 2-[2-(2-ethoxyethoxy)ethoxy]-.](data:image/png;base64,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)
![2-[2-[2-[2-[2-[2-[2-(2-Hydroxyethoxy)ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethanol.](data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAPoAAAD6CAIAAAAHjs1qAAANK0lEQVR4nO3Ze1CUZRvH8WsXEFfwkJIcNkwLTCsKKQWdMkZ90cqymcapt4YOWqhlvJM10snZmUbINI0O47RNkYxNFqP9sUxpI0J5QKnRJiUEFNQdeT0goSxy3N3f+8eDGxjLrjVvNnP9Pn+tOjfPtez3fu4HNAEQIh3MV3sAor8PcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyKhA/3jDz/I0KGSkiLvvisvvCCrVonZLCEhsny5mEx/14RXorlZ1q6V8HC5/np54omrPY0fR4/Kp59KWJikp8uMGVd7Gj927pTt28XtlieflAkTrvY0fnzxhdTVSXu7LFsmGzfKiy/KgQPicsk99/hbMWDuTU3i9YqI1NfLli1y550yZ45s3ChlZcF/TkePHr1w4cKJEyceeughsznYw8Tlcu3evdtsNqelpQ0fPjzIVfLuu7JkiVit8tprcvq0xMQEuW7fvn3Dhw93Op2zZ88O9loiDQ0Nx48fb2xsvP/++8PCwoJdtnatvPeeDBokCxZcUe4Oh+OGG25wu93JycnBrzp06BCAY8eOzZs3L/hVsmGDFBSI2y3PPScffxzkIrfbXVxcHBsba7Va4+Pjg79aSUmJ1Wptamq66667gl3T1CQ//yxr1siZM7JunbhcIiIXLkhz80CrMIAtW7BwIVauRFoa1qxBbS0A7N2Lzz5DS8tACwEAra2tNptt8ODBVqtVRCZNmrRz586Aq7xeb2FhYUxMTFhYmMViGTVqVH5+vtvtDrgQLS1YvLjntd2O/fuDGbKhoSErK8tsNk+YMEFEZs2aVVlZGXBVZ2dnfn7+0KFDo6KiRCQxMbG4uDjwhJcNuXQpWlrQ1RVw0eHDh+fMmSMi48ePN5vNmZmZp0+fDrjqt99+y87ODg0NHTt2rIhMmTJl7969gSfs7sbFi1iypOePixejpQVeb8B1O3bsSEpKEpHY2FiLxZKTk+NyuQKucjqdmZmZImJ8/+fOnXvs2LHAQ7pcOHQI77//+5BpaVi5EgsXYsuWAdYFyr20FACWLsWePVi9Gl4vXn0V33yDYcOQkwM/78fj8RQUFMTExIiI2WyeOXPmddddJyImk8mxbBmcTr9X3LPn0blzjX2YnJyckpJivE5JSRloqzQ0ICsLN96IDz/E1q3o6sKCBdi4EaNGIT8ffrZKe3v7ypUrIyIiRGTw4MEZGRnGMTJo0KDKvDycP+/vau7Nm5NuucUYbPr06QkJCcbr++67r7q62u+QVVWYMwezZmH5chw5guZmPP00VqxAYiKKivwtOnfu3JIlS0JCQkRk1KhRGRkZxjEyYsSI39av97tVurvP2u0jR44UkdDQ0IyMjGuvvdb4LJ599tkzZ874HXLHDiQlYflyLFyIpibU1+OllzBvHqZMgf+tcuTIEd/RMXbs2PT0dJPJJCK3jx/v/uorv1ulpWXf22+Hh4eLyNChQ2fPnj1kyBARGTJkiM1mu3jxYv+rvF4UFSE+HgUFeOopdHSgtBQffIClSwGgtPQv5F5djRMnAOC77wBg+3bk5mL3bqxaBZMJIhgzpnnzZm/f9/Pjjz9OnTrVePOTJ08uLy8H0NbWtmrVqsSYGE90NCyWfrZKQwMyM2EyFU+eHBcXZ7fbPR4PAIfDYdycjK1fX1/fe1FbW1t3Xh4iIiACiwXff49Nm/DWW6iuxuOPQwQimDSpec+ey96Z8WDg+7J1dXUAzp07l52dPTchAWFh/W+VqirMng2R3PT0iRMnbtu2DUBXV1d+fv6IESNEJCwsLDs7u7m5ufei5sZGLF6MkBCIICoKdXVYvx7vvINTp5Cc3DPkvfc219T0XtXd3W23243TIzQ0NCsrq7GxEUBtbe38+fNXp6VBpP+tUlKCpCSI/HvatBkzZhw8eBCAy+Wy2WxGW5GRkTabraOjo/ei80eP4sEHe4a5+WacOoW1a/Hhhzh+HKNHQwRmM555prnvVvEd4CISERFhs9na29sBVFRUpKWlld1zD0T62SpeLwoLERPjDglJvumm+fPnO51OACdPnszMzDS2itVqLSwsvCytlooKTJ7cM+TDD6O2Fm+9hc8/h9fbk+iJExjgjhMg9wFUVCAtDSL/SknxnZK9x42Li/vjuB1OJx55pGerJCWhoQGrV2P9etTU/J7sG2+0993ZxlaJjIwUEeOUbGlpAeBwOMaNG/dDejpEMHcu+u4EAHA4MG5cm8VyvdXq2ypVVVW+B3Rfsn2G/Pln3H13z/f0scdw6BDy8rBpE7Zt8yXbZbdf9nzV1NSUnZ1t3IZHjhxpPID5kv1vaipCQ5GVhcbGPhfr6oLdjqiouvj4yMhIX9MlJSW33nqrMeTMmTONZHvr3LYNN93UM2ReHsrKkJuLkhKsW9fzlwkJ7X94vjK2ivFlExMTi4qKcCnZ4RERHQkJiIiAzYb29j7LWlthsyE8fHtKitF0R0eH75nTOLQzMzNPnTrVe5HH4+n+9FNER/dsFYcDRUXIzcUvv+Dpp3uGnDq1/aefLhvS2CqX3S6NZ87boqO9w4YhLg52Ozyeyz/uIPzZ3AF4PCc2bhw9erRxSqamphqHkcViWbFiRWtrq9+FxlZZtw5PPAGXC9XVeOUVPPBA/8le4nQ6H330Ud9euu2224zvyIzUVE9Zmd9rtbWV5ef7BktNTTWKjIqK+uijjwb6kcDhwLhx+PprZGXB7UZxMex23HJLP8n2cuDAgenTpxuDjR8/3neAvPrYY6iq8nuts2c/fv1132B33HGHr0iHw+F3lbFV4uPx7bd4800AyMvD1q2IjYXNhr437962bt064dIvWyZNmuT7BL/MyUHfZPuoqfnPU0/5nlgmTpxovJ42bdpPf0j2d8ZWSUxEQQG2bIHbjUWL8O23sFoHSNbj8XzyySfR0dG+tIxnTovF8uPatRggrUD+Qu4ALt0bwsPDb7/99n6fN/rn8eD8eSxb1vPHRYvQ2RnM5SoqKqZOnWoymWJjY3030YCrfMdOcnJyWFiY7yYaQGcn9u7Fhg0A4PVi8eIghzSOncjISIvF4ruJBuQ7dhISEnw30aCGtNtx4AAAVFbi/feDGdJ37IwZM6b3TTQg49gZNGjQNddc0+/zht8hly7t+Ulj0yZ8/30wQ/7JtAb0V3M31NTU1NfX7969+wrWeL1YsAAA2trw/PPBr/N4PGVlZfv377/sETmg8vLy+vr6w4cPX8GakyexYgUAHDmC3Nzg17W1tZWXl+/ataszuB3iU1paWllZGcwvXn733Xf48ksA+PprBPkLIgDA2bNnDx48WFpaGlSyl3R1de3cuXPfvn0DHeB/tGYNfv0VAN58E8H87uWS2traurq6Xbt2XcG1/DMBkKulpER27ZKuLlm0SC79PPqPU1goTqd0d8vLL8uwYVd7mv4Asnq1eDxiMklOjgT9nxt/q9ZWWbNGQkMlLk4WLrxaU1zV3In+Xv/IOwHR/wdzJ0WYOynC3EkR5k6KMHdShLmTIsydFGHupAhzJ0WYOynC3EkR5k6KMHdShLmTIsydFGHupAhzJ0WYOynC3EkR5k6KMHdShLmTIsydFGHupAhzJ0WYOynC3EkR5k6KMHdShLmTIsydFGHupAhzJ0WYOynC3EkR5k6KMHdShLmTIsydFGHupAhzJ0WYOynC3EkR5k6KMHdShLmTIsydFGHupAhzJ0WYOynC3EkR5k6KMHdShLmTIsydFGHupAhzJ0WYOynC3EkR5k6KMHdShLmTIsydFGHupAhzJ0WYOynC3EkR5k6KMHdShLmTIsydFGHupAhzJ0WYOynC3EkR5k6KMHdShLmTIsydFGHupAhzJ0WYOynC3EkR5k6KMHdShLmTIsydFGHupAhzJ0WYOynC3EkR5k6KMHdShLmTIsydFGHupAhzJ0WYOynC3EkR5k6KMHdShLmTIsydFGHupAhzJ0WYOynC3EkR5k6KMHdShLmTIsydFGHupAhzJ0WYOynC3EkR5k6KMHdShLmTIv8DmnJ84cAsyoIAAAAASUVORK5CYII=)
![2-[2-[2-[2-[2-[2-[2-[2-[2-[2-[2-(2-Hydroxyethoxy)ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethanol.](data:image/png;base64,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)
Find more compounds similar to Ethanol, 2-(2-ethoxyethoxy)-.
Mixtures
- Ethanol, 2-(2-ethoxyethoxy)- + Propylamine
- Ethanol, 2-(2-ethoxyethoxy)- + Propane, 2-ethoxy-2-methyl-
- Ethanol, 2-(2-ethoxyethoxy)- + Water
- Ethanol, 2-(2-ethoxyethoxy)- + Ethanol
- Ethanol, 2-(2-ethoxyethoxy)- + Formamide, N,N-dimethyl-
- Ethanol, 2-(2-ethoxyethoxy)- + Benzyl alcohol
- Ethanol, 2-(2-ethoxyethoxy)- + 1-Hexanol
- Ethanol, 2-(2-ethoxyethoxy)- + 1-Octanol
- Ethanol, 2-(2-ethoxyethoxy)- + 1-Decanol
- Ethanol, 2-(2-ethoxyethoxy)- + Acetaminophen + Water
- Ethanol, 2-(2-ethoxyethoxy)- + Acetaminophen
- Ethanol, 2-(2-ethoxyethoxy)- + 1H-Indole-2,3-dione
Sources
- Crippen Method
- Crippen Method
- Speeds of Sound and Isentropic Compressibilities of n-Alkoxyethanols and Polyethers with Propylamine at 298.15K
- Viscosities of binary mixtures of some n-ethoxyethanols with ethyl tert-butyl ether at T = (293.15, 298.15, and 303.15) K
- Density and refractive index in mixtures of ionic liquids and organic solvents: Correlations and predictions
- Thermodynamic and optical studies of some ethylene glycol ethers in aqueous solutions at T = 298.15 K
- Volumetric, acoustic, and viscometric studies of molecular interactions in binary mixtures of diethylene glycol monomethyl ether with 1-alkanols at temperatures from (293.15 to 308.15) K
- Volumetric and viscometric study of aqueous binary mixtures of some glycol ethers at T = (275.15 and 283.15) K
- Thermodynamics of the solubility of reserpine in {{2-(2-ethoxyethoxy)ethanol + water}} mixed solvent systems at different temperatures
- Solubility and thermodynamic function of a new anticancer drug ibrutinib in 2-(2-ethoxyethoxy)ethanol + water mixtures at different temperatures
- Solubility and thermodynamic function of a bioactive compound bergenin in various pharmaceutically acceptable neat solvents at different temperatures
- Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
- Solubility and Thermodynamic Analysis of Tenoxicam in Different Pure Solvents at Different Temperatures
- Thermophysical properties of glycols and glymes
- Density, Speed of Sound, and Viscosity of Diethylene Glycol Monoethyl Ether + N,N-Dimethylformamide (Ethanol, Water) at T = 288.15-318.15 K
- Liquid Density Measurements of Diethylene Glycol Monoalkyl Ethers as a Function of Temperature and Pressure
- Excess Molar Enthalpies and Hydrogen Bonding in Binary Mixtures Containing Ethers and Benzyl Alcohol at 308.15 K and Atmospheric Pressure
- Solubilization Behavior of Paracetamol in Transcutol Water Mixtures at (298.15 to 333.15) K
- Measurement and Correlation of Tadalafil Solubility in Five Pure Solvents at (298.15 to 333.15) K
- Solubility of Metoclopramide Hydrochloride in Six Green Solvents at (298.15 to 338.15) K
- Solubility of N-(4-Chlorophenyl)-2-(pyridin-4-ylcarbonyl)hydrazinecarbothioamide (Isoniazid Analogue) in Transcutol + Water Cosolvent Mixtures at (298.15 to 338.15) K
- Solubility of (2Z)-N-Cyclohexyl-2-(3-hydroxybenzylidine) Hydrazine Carbothioamide in Different Pure Solvents at (298.15 to 338.15) K
- Solubility of N-(4-Chlorophenyl)-2-(pyridin-4-ylcarbonyl)hydrazinecarbothioamide (Isoniazid Analogue) in Five Pure Solvents at (298.15 to 338.15) K
- Correlation of Solubility of Bioactive Compound Reserpine in Eight Green Solvents at (298.15 to 338.15) K
- Measurement, Correlation, and Thermodynamics of Solubility of Isatin in Nine Different Green Solvents at (298.15 to 338.15) K
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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