- InChI
- InChI=1S/C6H14O4/c7-1-3-9-5-6-10-4-2-8/h7-8H,1-6H2
- InChI Key
- ZIBGPFATKBEMQZ-UHFFFAOYSA-N
- Formula
- C6H14O4
- SMILES
- OCCOCCOCCO
- Molecular Weight1
- 150.17
- CAS
- 112-27-6
- Other Names
-
- 1,2-BIS(2-HYDROXYETHOXY)ETHANE
- 1,2-di(.beta.-hydroxyethoxy)ethane
- 2,2'-(1,2-Ethanediylbis(oxy))bisethanol
- 2,2'-(ethane-1,2-diylbis(oxy))bis(ethan-1-ol)
- 2,2'-(ethylenedioxy)diethanol
- 2,2'-Ethylenedioxybis(ethanol)
- 2,2'-Ethylenedioxydiethanol
- 2,2'-Ethylenedioxyethanol
- 2-(2-(2-hydroxyethoxy)ethoxy)ethanol
- 3,6-Dioxaoctane-1,8-diol
- 3,6-dioxa-1,8-octanediol
- Di-«beta»-hydroxyethoxyethane
- Di-«beta»-hydroxyethoxyethane
- Ethanol, 2,2'-(ethylenedioxy)di-
- Ethanol, 2,2'-[1,2-ethanediylbis(oxy)]bis-
- Ethylene glycol dihydroxydiethyl ether
- Ethylene glycol-bis-(2-hydroxyethyl ether)
- Glycol bis(hydroxyethyl) ether
- NSC 60758
- TEG
- TRIGEN
- Triethylenglykol
- Trigenos
- Triglycol
- Trigol
- ethylene glycol bis(2-hydroxyethyl) ether
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- 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).
- μJT : Joule-Thomson coefficient (K/kPa).
- NFPA Fire : NFPA Fire Rating.
- NFPA Health : NFPA Health Rating.
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- Tboil : Normal Boiling Point Temperature (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
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°liquid | -3557.60 ± 3.60 | kJ/mol | NIST |
| ΔfG° | -484.00 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -736.07 | kJ/mol | Joback Calculated Property |
| ΔfH°liquid | -804.20 ± 3.60 | kJ/mol | NIST |
| ΔfusH° | 21.85 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 60.50 | kJ/mol | NIST |
| log10WS | 0.96 | Crippen Calculated Property | |
| logPoct/wat | -0.996 | Crippen Calculated Property | |
| McVol | 118.880 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 1 | KDB | |
| NFPA Health | 1 | KDB | |
| Pc | 3300.00 ± 60.00 | kPa | NIST |
| Inp | [206.80; 1177.00] |
|
|
| Inp | 1143.00 | NIST | |
| Inp | 1177.00 | NIST | |
| Inp | 206.80 | NIST | |
| Inp | 206.80 | NIST | |
| Tboil | [439.00; 571.60] | K |
|
| Tboil | 558.20 | K | NIST |
| Tboil | 551.50 | K | NIST |
| Tboil | 549.00 ± 2.00 | K | NIST |
| Tboil | Outlier 439.00 ± 5.00 | K | NIST |
| Tboil | 571.60 ± 1.00 | K | NIST |
| Tboil | 561.15 | K | NIST |
| Tboil | 549.00 ± 3.00 | K | NIST |
| Tc | [713.00; 797.00] | K |
|
| Tc | 788.00 | K | Critica... |
| Tc | 797.00 ± 10.00 | K | NIST |
| Tc | 713.00 ± 20.00 | K | NIST |
| Tfus | [263.75; 268.85] | K |
|
| Tfus | 268.85 | K | NIST |
| Tfus | 263.75 ± 0.50 | K | NIST |
| Vc | 0.446 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [299.99; 346.71] | J/mol×K | [565.88; 723.89] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 300 310 320 330 340 350 600 650 700 | ||||
| Cp,gas | 299.99 | J/mol×K | 565.88 | Joback Calculated Property |
| Cp,gas | 308.46 | J/mol×K | 592.21 | Joback Calculated Property |
| Cp,gas | 316.66 | J/mol×K | 618.55 | Joback Calculated Property |
| Cp,gas | 324.59 | J/mol×K | 644.88 | Joback Calculated Property |
| Cp,gas | 332.24 | J/mol×K | 671.22 | Joback Calculated Property |
| Cp,gas | 339.62 | J/mol×K | 697.55 | Joback Calculated Property |
| Cp,gas | 346.71 | J/mol×K | 723.89 | Joback Calculated Property |
| Cp,liquid | [327.60; 359.30] | J/mol×K | [298.00; 353.15] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 325 330 335 340 345 350 355 360 300 320 340 | ||||
| Cp,liquid | 333.70 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 327.60 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 336.30 | J/mol×K | 303.15 | Heat ca... |
| Cp,liquid | 339.50 | J/mol×K | 313.15 | Heat ca... |
| Cp,liquid | 343.10 | J/mol×K | 323.15 | Heat ca... |
| Cp,liquid | 347.90 | J/mol×K | 333.15 | Heat ca... |
| Cp,liquid | 353.70 | J/mol×K | 343.15 | Heat ca... |
| Cp,liquid | 359.30 | J/mol×K | 353.15 | Heat ca... |
| η | [0.0009970; 0.0483200] | Pa×s | [293.20; 462.25] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 0.01 0.02 0.03 0.04 0.05 300 350 400 450 | ||||
| η | 0.0483200 | Pa×s | 293.20 | Phase e... |
| η | 0.0368200 | Pa×s | 298.15 | Experim... |
| η | 0.0343980 | Pa×s | 298.15 | Densiti... |
| η | 0.0300120 | Pa×s | 298.15 | Thermop... |
| η | 0.0371600 | Pa×s | 298.20 | Phase e... |
| η | 0.0351000 | Pa×s | 299.65 | Density... |
| η | 0.0292700 | Pa×s | 303.15 | Vapour ... |
| η | 0.0292700 | Pa×s | 303.20 | Phase e... |
| η | 0.0169720 | Pa×s | 308.15 | Thermop... |
| η | 0.0213060 | Pa×s | 308.15 | Densiti... |
| η | 0.0237400 | Pa×s | 308.20 | Phase e... |
| η | 0.0190300 | Pa×s | 312.96 | Experim... |
| η | 0.0195000 | Pa×s | 313.05 | Density... |
| η | 0.0189600 | Pa×s | 313.15 | Vapour ... |
| η | 0.0192600 | Pa×s | 313.20 | Phase e... |
| η | 0.0164100 | Pa×s | 318.20 | Phase e... |
| η | 0.0129600 | Pa×s | 323.15 | Vapour ... |
| η | 0.0135100 | Pa×s | 323.20 | Phase e... |
| η | 0.0113500 | Pa×s | 328.20 | Phase e... |
| η | 0.0096600 | Pa×s | 333.10 | Density... |
| η | 0.0092880 | Pa×s | 333.15 | Vapour ... |
| η | 0.0096020 | Pa×s | 333.20 | Phase e... |
| η | 0.0090020 | Pa×s | 334.96 | Experim... |
| η | 0.0082780 | Pa×s | 338.20 | Phase e... |
| η | 0.0069060 | Pa×s | 343.15 | Vapour ... |
| η | 0.0073510 | Pa×s | 343.20 | Phase e... |
| η | 0.0059450 | Pa×s | 349.25 | Experim... |
| η | 0.0055500 | Pa×s | 353.05 | Density... |
| η | 0.0041310 | Pa×s | 364.44 | Experim... |
| η | 0.0034100 | Pa×s | 373.50 | Density... |
| η | 0.0023600 | Pa×s | 393.30 | Density... |
| η | 0.0017100 | Pa×s | 413.25 | Density... |
| η | 0.0016790 | Pa×s | 413.73 | Experim... |
| η | 0.0013900 | Pa×s | 428.10 | Density... |
| η | 0.0009970 | Pa×s | 462.25 | Experim... |
| ΔvapH | [60.80; 79.20] | kJ/mol | [273.00; 502.00] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 60 65 70 75 80 300 400 500 | ||||
| ΔvapH | 79.20 ± 7.90 | kJ/mol | 273.00 | NIST |
| ΔvapH | 67.70 | kJ/mol | 295.50 | NIST |
| ΔvapH | 77.00 | kJ/mol | 300.50 | NIST |
| ΔvapH | 71.50 | kJ/mol | 469.50 | NIST |
| ΔvapH | 64.60 ± 0.30 | kJ/mol | 502.00 | NIST |
| ΔvapH | 60.80 ± 0.50 | kJ/mol | 502.00 | NIST |
| ΔvapH | 72.20 ± 0.30 | kJ/mol | 502.00 | NIST |
| ΔvapH | 68.50 ± 0.30 | kJ/mol | 502.00 | NIST |
| n0 | [1.45314; 1.45560] | [293.15; 293.15] |
|
|
| n0 | 1.45560 | 293.15 | Infinit... | |
| n0 | 1.45314 | 293.15 | Liquid-... | |
| ρl | [1061.90; 1135.14] | kg/m3 | [278.15; 373.15] |
|
|
T(K) Liquid Density (kg/m3) 1060 1080 1100 1120 1140 300 350 | ||||
| ρl | 1135.14 | kg/m3 | 278.15 | Acousti... |
| ρl | 1131.30 | kg/m3 | 283.15 | Thermop... |
| ρl | 1131.29 | kg/m3 | 283.15 | Acousti... |
| ρl | 1127.37 | kg/m3 | 288.15 | Activit... |
| ρl | 1127.40 | kg/m3 | 288.15 | Thermop... |
| ρl | 1128.60 | kg/m3 | 288.15 | Thermop... |
| ρl | 1127.43 | kg/m3 | 288.15 | Acousti... |
| ρl | 1124.60 | kg/m3 | 293.15 | Thermop... |
| ρl | 1124.50 | kg/m3 | 293.15 | Measure... |
| ρl | 1123.50 | kg/m3 | 293.15 | Thermop... |
| ρl | 1124.60 | kg/m3 | 293.15 | Experim... |
| ρl | 1123.56 | kg/m3 | 293.15 | Acousti... |
| ρl | 1124.70 | kg/m3 | 293.15 | Density... |
| ρl | 1124.60 | kg/m3 | 293.15 | Measure... |
| ρl | 1123.48 | kg/m3 | 293.15 | Thermod... |
| ρl | 1123.20 | kg/m3 | 293.35 | Measure... |
| ρl | 1116.05 | kg/m3 | 298.00 | Removal... |
| ρl | 1120.70 | kg/m3 | 298.15 | Isobari... |
| ρl | 1119.78 | kg/m3 | 298.15 | Excess ... |
| ρl | 1120.80 | kg/m3 | 298.15 | Experim... |
| ρl | 1119.70 | kg/m3 | 298.15 | Thermop... |
| ρl | 1120.80 | kg/m3 | 298.15 | Measure... |
| ρl | 1120.70 | kg/m3 | 298.15 | Thermop... |
| ρl | 1119.69 | kg/m3 | 298.15 | Acousti... |
| ρl | 1119.78 | kg/m3 | 298.15 | Thermod... |
| ρl | 1119.59 | kg/m3 | 298.15 | Thermod... |
| ρl | 1116.60 | kg/m3 | 302.85 | Measure... |
| ρl | 1116.50 | kg/m3 | 303.15 | Density... |
| ρl | 1116.80 | kg/m3 | 303.15 | Thermop... |
| ρl | 1115.81 | kg/m3 | 303.15 | Acousti... |
| ρl | 1117.00 | kg/m3 | 303.15 | Density... |
| ρl | 1116.90 | kg/m3 | 303.15 | Measure... |
| ρl | 1115.80 | kg/m3 | 303.15 | Thermop... |
| ρl | 1115.70 | kg/m3 | 303.15 | Thermod... |
| ρl | 1111.90 | kg/m3 | 307.75 | Measure... |
| ρl | 1113.00 | kg/m3 | 308.15 | Experim... |
| ρl | 1111.81 | kg/m3 | 308.15 | Thermod... |
| ρl | 1112.09 | kg/m3 | 308.15 | Excess ... |
| ρl | 1112.10 | kg/m3 | 308.15 | Excess ... |
| ρl | 1113.00 | kg/m3 | 308.15 | Measure... |
| ρl | 1112.61 | kg/m3 | 308.15 | Thermod... |
| ρl | 1111.92 | kg/m3 | 308.15 | Acousti... |
| ρl | 1112.61 | kg/m3 | 308.15 | Excess ... |
| ρl | 1111.90 | kg/m3 | 308.15 | Thermop... |
| ρl | 1112.90 | kg/m3 | 308.15 | Thermop... |
| ρl | 1112.59 | kg/m3 | 308.50 | Excess ... |
| ρl | 1108.40 | kg/m3 | 312.65 | Measure... |
| ρl | 1108.00 | kg/m3 | 313.15 | Thermop... |
| ρl | 1109.10 | kg/m3 | 313.15 | Measure... |
| ρl | 1109.00 | kg/m3 | 313.15 | Thermop... |
| ρl | 1108.03 | kg/m3 | 313.15 | Acousti... |
| ρl | 1109.20 | kg/m3 | 313.15 | Density... |
| ρl | 1108.90 | kg/m3 | 313.15 | Density... |
| ρl | 1104.70 | kg/m3 | 317.45 | Measure... |
| ρl | 1105.10 | kg/m3 | 318.15 | Thermop... |
| ρl | 1105.20 | kg/m3 | 318.15 | Measure... |
| ρl | 1105.20 | kg/m3 | 318.15 | Experim... |
| ρl | 1104.13 | kg/m3 | 318.15 | Acousti... |
| ρl | 1101.00 | kg/m3 | 322.25 | Measure... |
| ρl | 1101.30 | kg/m3 | 323.15 | Measure... |
| ρl | 1101.50 | kg/m3 | 323.15 | Density... |
| ρl | 1101.10 | kg/m3 | 323.15 | Density... |
| ρl | 1100.22 | kg/m3 | 323.15 | Acousti... |
| ρl | 1101.20 | kg/m3 | 323.15 | Thermop... |
| ρl | 1100.20 | kg/m3 | 323.15 | Thermop... |
| ρl | 1097.90 | kg/m3 | 327.05 | Measure... |
| ρl | 1096.30 | kg/m3 | 328.15 | Acousti... |
| ρl | 1097.40 | kg/m3 | 328.15 | Experim... |
| ρl | 1097.30 | kg/m3 | 328.15 | Thermop... |
| ρl | 1097.40 | kg/m3 | 328.15 | Measure... |
| ρl | 1093.50 | kg/m3 | 332.15 | Measure... |
| ρl | 1093.70 | kg/m3 | 333.15 | Density... |
| ρl | 1092.38 | kg/m3 | 333.15 | Acousti... |
| ρl | 1092.40 | kg/m3 | 333.15 | Thermop... |
| ρl | 1093.50 | kg/m3 | 333.15 | Measure... |
| ρl | 1093.40 | kg/m3 | 333.15 | Thermop... |
| ρl | 1093.40 | kg/m3 | 333.15 | Density... |
| ρl | 1089.60 | kg/m3 | 338.15 | Measure... |
| ρl | 1089.50 | kg/m3 | 338.15 | Thermop... |
| ρl | 1086.10 | kg/m3 | 341.45 | Measure... |
| ρl | 1085.60 | kg/m3 | 343.15 | Measure... |
| ρl | 1085.90 | kg/m3 | 343.15 | Density... |
| ρl | 1085.50 | kg/m3 | 343.15 | Density... |
| ρl | 1085.60 | kg/m3 | 343.15 | Thermop... |
| ρl | 1084.50 | kg/m3 | 343.15 | Thermop... |
| ρl | 1085.60 | kg/m3 | 343.15 | Experim... |
| ρl | 1081.70 | kg/m3 | 348.15 | Thermop... |
| ρl | 1077.80 | kg/m3 | 353.15 | Thermop... |
| ρl | 1073.80 | kg/m3 | 358.15 | Thermop... |
| ρl | 1069.80 | kg/m3 | 363.15 | Thermop... |
| ρl | 1065.90 | kg/m3 | 368.15 | Thermop... |
| ρl | 1061.90 | kg/m3 | 373.15 | Thermop... |
| λ | [0.19; 0.19] | W/m×K | [298.10; 338.40] |
|
|
T(K) Liquid thermal conductivity (W/m×K) 0.19 0.19 0.19 0.19 0.19 300 310 320 330 | ||||
| λ | 0.19 | W/m×K | 298.10 | Applica... |
| λ | 0.19 | W/m×K | 308.20 | Applica... |
| λ | 0.19 | W/m×K | 318.40 | Applica... |
| λ | 0.19 | W/m×K | 328.40 | Applica... |
| λ | 0.19 | W/m×K | 338.40 | Applica... |
Datasets
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 298.15 | 98.00 | 0.0368 |
| 298.15 | 49030.00 | 0.0552 |
| 298.15 | 98060.00 | 0.0803 |
| 298.15 | 147100.00 | 0.1144 |
| 298.15 | 196130.00 | 0.1606 |
| 298.15 | 245160.00 | 0.2218 |
| 312.96 | 98.00 | 0.0190 |
| 313.05 | 49030.00 | 0.0274 |
| 313.10 | 98060.00 | 0.0383 |
| 313.18 | 147100.00 | 0.0525 |
| 313.25 | 196130.00 | 0.0707 |
| 313.26 | 245160.00 | 0.0940 |
| 334.96 | 98.00 | 0.0090 |
| 335.11 | 49030.00 | 0.0124 |
| 335.14 | 98060.00 | 0.0167 |
| 335.20 | 147100.00 | 0.0220 |
| 335.25 | 196130.00 | 0.0285 |
| 335.26 | 245160.00 | 0.0364 |
| 349.25 | 98.00 | 0.0059 |
| 349.94 | 196130.00 | 0.0175 |
| 349.98 | 49030.00 | 0.0081 |
| 349.98 | 98060.00 | 0.0107 |
| 349.99 | 245160.00 | 0.0218 |
| 350.03 | 147100.00 | 0.0138 |
| 364.44 | 98.00 | 0.0041 |
| 364.44 | 49030.00 | 0.0055 |
| 364.72 | 98060.00 | 0.0071 |
| 365.03 | 147100.00 | 0.0090 |
| 365.07 | 196130.00 | 0.0112 |
| 365.20 | 245160.00 | 0.0138 |
| 413.73 | 98.00 | 0.0017 |
| 414.00 | 49030.00 | 0.0022 |
| 414.15 | 98060.00 | 0.0028 |
| 414.27 | 147100.00 | 0.0033 |
| 414.30 | 196130.00 | 0.0040 |
| 414.43 | 245160.00 | 0.0045 |
| 462.25 | 98.00 | 0.0010 |
| 462.26 | 49030.00 | 0.0013 |
| 462.32 | 98060.00 | 0.0016 |
| 462.41 | 147100.00 | 0.0019 |
| 462.45 | 196130.00 | 0.0023 |
| 462.58 | 245160.00 | 0.0027 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Viscosity, Pa*s - Liquid |
| 101.30 | 308.15 | 0.0238 |
| Reference | ||
Joule-Thomson coefficient, K/kPa
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Joule-Thomson coefficient, K/kPa - Liquid |
| 293.10 | 7000.00 | -0.0004 |
| Reference | ||
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 283.08 | 100.00 | 1131.7 |
| 283.08 | 1000.00 | 1132.4 |
| 283.08 | 2000.00 | 1132.8 |
| 283.08 | 5000.00 | 1134.1 |
| 283.08 | 7000.00 | 1134.9 |
| 283.08 | 10000.00 | 1136.2 |
| 283.08 | 12000.00 | 1137.1 |
| 283.08 | 16000.00 | 1138.8 |
| 283.08 | 20000.00 | 1140.5 |
| 283.08 | 25000.00 | 1142.5 |
| 283.08 | 30000.00 | 1144.5 |
| 283.08 | 35000.00 | 1146.5 |
| 283.08 | 40000.00 | 1148.4 |
| 283.08 | 45000.00 | 1150.2 |
| 283.08 | 50000.00 | 1152.1 |
| 283.08 | 55000.00 | 1154.0 |
| 283.08 | 60000.00 | 1155.8 |
| 283.08 | 65000.00 | 1157.6 |
| 283.08 | 70000.00 | 1159.4 |
| 283.08 | 75000.00 | 1161.0 |
| 283.08 | 80000.00 | 1162.8 |
| 283.08 | 85000.00 | 1164.5 |
| 283.08 | 90000.00 | 1166.1 |
| 283.08 | 95000.00 | 1167.7 |
| 293.14 | 100.00 | 1124.1 |
| 293.14 | 1000.00 | 1124.5 |
| 293.14 | 2000.00 | 1124.9 |
| 293.14 | 5000.00 | 1126.3 |
| 293.14 | 7000.00 | 1127.3 |
| 293.14 | 10000.00 | 1128.6 |
| 293.14 | 12000.00 | 1129.4 |
| 293.14 | 16000.00 | 1131.3 |
| 293.14 | 20000.00 | 1132.9 |
| 293.14 | 25000.00 | 1135.0 |
| 293.14 | 30000.00 | 1137.1 |
| 293.14 | 35000.00 | 1139.2 |
| 293.14 | 40000.00 | 1141.1 |
| 293.14 | 45000.00 | 1143.0 |
| 293.14 | 50000.00 | 1145.0 |
| 293.14 | 55000.00 | 1146.9 |
| 293.14 | 60000.00 | 1148.7 |
| 293.14 | 65000.00 | 1150.5 |
| 293.14 | 70000.00 | 1152.4 |
| 293.14 | 75000.00 | 1154.2 |
| 293.14 | 80000.00 | 1155.9 |
| 293.14 | 85000.00 | 1157.6 |
| 293.14 | 90000.00 | 1159.2 |
| 293.14 | 95000.00 | 1160.9 |
| 303.12 | 100.00 | 1116.2 |
| 303.12 | 1000.00 | 1116.6 |
| 303.12 | 2000.00 | 1117.1 |
| 303.12 | 5000.00 | 1118.5 |
| 303.12 | 7000.00 | 1119.5 |
| 303.12 | 10000.00 | 1120.9 |
| 303.12 | 12000.00 | 1121.8 |
| 303.12 | 16000.00 | 1123.6 |
| 303.12 | 20000.00 | 1125.4 |
| 303.12 | 25000.00 | 1127.6 |
| 303.12 | 30000.00 | 1129.7 |
| 303.12 | 35000.00 | 1131.8 |
| 303.12 | 40000.00 | 1133.9 |
| 303.12 | 45000.00 | 1135.9 |
| 303.12 | 50000.00 | 1137.9 |
| 303.12 | 55000.00 | 1139.9 |
| 303.12 | 60000.00 | 1141.8 |
| 303.12 | 65000.00 | 1143.7 |
| 303.12 | 70000.00 | 1145.5 |
| 303.12 | 75000.00 | 1147.3 |
| 303.12 | 80000.00 | 1149.1 |
| 303.12 | 85000.00 | 1150.8 |
| 303.12 | 90000.00 | 1152.6 |
| 303.12 | 95000.00 | 1154.2 |
| 313.18 | 100.00 | 1108.3 |
| 313.18 | 1000.00 | 1108.7 |
| 313.18 | 2000.00 | 1109.2 |
| 313.18 | 5000.00 | 1110.7 |
| 313.18 | 7000.00 | 1111.7 |
| 313.18 | 10000.00 | 1113.1 |
| 313.18 | 12000.00 | 1114.1 |
| 313.18 | 16000.00 | 1115.9 |
| 313.18 | 20000.00 | 1117.8 |
| 313.18 | 25000.00 | 1120.0 |
| 313.18 | 30000.00 | 1122.3 |
| 313.18 | 35000.00 | 1124.4 |
| 313.18 | 40000.00 | 1126.6 |
| 313.18 | 45000.00 | 1128.7 |
| 313.18 | 50000.00 | 1130.6 |
| 313.18 | 55000.00 | 1132.6 |
| 313.18 | 60000.00 | 1134.6 |
| 313.18 | 65000.00 | 1136.6 |
| 313.18 | 70000.00 | 1138.5 |
| 313.18 | 75000.00 | 1140.3 |
| 313.18 | 80000.00 | 1142.1 |
| 313.18 | 85000.00 | 1143.9 |
| 313.18 | 90000.00 | 1145.6 |
| 313.18 | 95000.00 | 1147.4 |
| 323.14 | 100.00 | 1100.5 |
| 323.14 | 1000.00 | 1101.0 |
| 323.14 | 2000.00 | 1101.5 |
| 323.14 | 5000.00 | 1103.0 |
| 323.14 | 7000.00 | 1104.1 |
| 323.14 | 10000.00 | 1105.5 |
| 323.14 | 12000.00 | 1106.5 |
| 323.14 | 16000.00 | 1108.4 |
| 323.14 | 20000.00 | 1110.3 |
| 323.14 | 25000.00 | 1112.6 |
| 323.14 | 30000.00 | 1114.9 |
| 323.14 | 35000.00 | 1117.1 |
| 323.14 | 40000.00 | 1119.4 |
| 323.14 | 45000.00 | 1121.5 |
| 323.14 | 50000.00 | 1123.7 |
| 323.14 | 55000.00 | 1125.7 |
| 323.14 | 60000.00 | 1127.7 |
| 323.14 | 65000.00 | 1129.7 |
| 323.14 | 70000.00 | 1131.7 |
| 323.14 | 75000.00 | 1133.5 |
| 323.14 | 80000.00 | 1135.4 |
| 323.14 | 85000.00 | 1137.3 |
| 323.14 | 90000.00 | 1139.0 |
| 323.14 | 95000.00 | 1140.8 |
| 333.10 | 100.00 | 1092.7 |
| 333.10 | 1000.00 | 1093.2 |
| 333.10 | 2000.00 | 1093.8 |
| 333.10 | 5000.00 | 1095.4 |
| 333.10 | 7000.00 | 1096.4 |
| 333.10 | 10000.00 | 1098.0 |
| 333.10 | 12000.00 | 1098.9 |
| 333.10 | 16000.00 | 1100.9 |
| 333.10 | 20000.00 | 1102.9 |
| 333.10 | 25000.00 | 1105.3 |
| 333.10 | 30000.00 | 1107.7 |
| 333.10 | 35000.00 | 1110.1 |
| 333.10 | 40000.00 | 1112.3 |
| 333.10 | 45000.00 | 1114.5 |
| 333.10 | 50000.00 | 1116.6 |
| 333.10 | 55000.00 | 1118.9 |
| 333.10 | 60000.00 | 1120.8 |
| 333.10 | 65000.00 | 1122.9 |
| 333.10 | 70000.00 | 1124.9 |
| 333.10 | 75000.00 | 1126.9 |
| 333.10 | 80000.00 | 1128.8 |
| 333.10 | 85000.00 | 1130.7 |
| 333.10 | 90000.00 | 1132.5 |
| 333.10 | 95000.00 | 1134.4 |
| 343.14 | 100.00 | 1084.7 |
| 343.14 | 1000.00 | 1085.3 |
| 343.14 | 2000.00 | 1086.0 |
| 343.14 | 5000.00 | 1087.6 |
| 343.14 | 7000.00 | 1088.6 |
| 343.14 | 10000.00 | 1090.2 |
| 343.14 | 12000.00 | 1091.3 |
| 343.14 | 16000.00 | 1093.4 |
| 343.14 | 20000.00 | 1095.4 |
| 343.14 | 25000.00 | 1097.9 |
| 343.14 | 30000.00 | 1100.4 |
| 343.14 | 35000.00 | 1102.8 |
| 343.14 | 40000.00 | 1105.1 |
| 343.14 | 45000.00 | 1107.4 |
| 343.14 | 50000.00 | 1109.6 |
| 343.14 | 55000.00 | 1111.9 |
| 343.14 | 60000.00 | 1114.0 |
| 343.14 | 65000.00 | 1116.1 |
| 343.14 | 70000.00 | 1118.1 |
| 343.14 | 75000.00 | 1120.1 |
| 343.14 | 80000.00 | 1122.1 |
| 343.14 | 85000.00 | 1124.1 |
| 343.14 | 90000.00 | 1126.0 |
| 343.14 | 95000.00 | 1128.0 |
| 353.10 | 100.00 | 1077.0 |
| 353.10 | 1000.00 | 1076.9 |
| 353.10 | 2000.00 | 1078.0 |
| 353.10 | 5000.00 | 1079.8 |
| 353.10 | 7000.00 | 1080.9 |
| 353.10 | 10000.00 | 1082.6 |
| 353.10 | 12000.00 | 1083.6 |
| 353.10 | 16000.00 | 1085.7 |
| 353.10 | 20000.00 | 1088.0 |
| 353.10 | 25000.00 | 1090.5 |
| 353.10 | 30000.00 | 1093.2 |
| 353.10 | 35000.00 | 1095.5 |
| 353.10 | 40000.00 | 1098.0 |
| 353.10 | 45000.00 | 1100.3 |
| 353.10 | 50000.00 | 1102.6 |
| 353.10 | 55000.00 | 1104.9 |
| 353.10 | 60000.00 | 1107.3 |
| 353.10 | 65000.00 | 1109.1 |
| 353.10 | 70000.00 | 1111.5 |
| 353.10 | 75000.00 | 1113.3 |
| 353.10 | 80000.00 | 1115.6 |
| 353.10 | 85000.00 | 1117.4 |
| 353.10 | 90000.00 | 1119.5 |
| 353.10 | 95000.00 | 1121.3 |
| 363.16 | 100.00 | 1068.9 |
| 363.16 | 1000.00 | 1069.4 |
| 363.16 | 2000.00 | 1070.1 |
| 363.16 | 5000.00 | 1071.8 |
| 363.16 | 7000.00 | 1073.0 |
| 363.16 | 10000.00 | 1074.6 |
| 363.16 | 12000.00 | 1075.8 |
| 363.16 | 16000.00 | 1078.2 |
| 363.16 | 20000.00 | 1080.3 |
| 363.16 | 25000.00 | 1082.9 |
| 363.16 | 30000.00 | 1085.6 |
| 363.16 | 35000.00 | 1088.1 |
| 363.16 | 40000.00 | 1090.6 |
| 363.16 | 45000.00 | 1093.0 |
| 363.16 | 50000.00 | 1095.4 |
| 363.16 | 55000.00 | 1097.8 |
| 363.16 | 60000.00 | 1100.1 |
| 363.16 | 65000.00 | 1102.3 |
| 363.16 | 70000.00 | 1104.5 |
| 363.16 | 75000.00 | 1106.6 |
| 363.16 | 80000.00 | 1108.7 |
| 363.16 | 85000.00 | 1110.7 |
| 363.16 | 90000.00 | 1112.8 |
| 363.16 | 95000.00 | 1114.8 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 283.15 | 100.00 | 1130.8 |
| 283.15 | 100.00 | 1130.8 |
| 283.15 | 660.00 | 1131.0 |
| 283.15 | 1150.00 | 1131.2 |
| 283.15 | 1570.00 | 1131.4 |
| 283.15 | 2090.00 | 1131.6 |
| 283.15 | 3090.00 | 1132.0 |
| 283.15 | 5060.00 | 1132.9 |
| 283.15 | 6940.00 | 1133.6 |
| 283.15 | 10020.00 | 1134.9 |
| 283.15 | 14850.00 | 1136.9 |
| 283.15 | 19830.00 | 1138.9 |
| 283.15 | 24700.00 | 1140.8 |
| 283.15 | 29600.00 | 1142.7 |
| 283.15 | 34510.00 | 1144.6 |
| 283.15 | 39360.00 | 1146.4 |
| 283.15 | 44290.00 | 1148.2 |
| 283.15 | 49180.00 | 1150.0 |
| 283.15 | 54110.00 | 1151.7 |
| 283.15 | 58970.00 | 1153.4 |
| 283.15 | 63860.00 | 1155.1 |
| 283.15 | 68790.00 | 1156.8 |
| 293.15 | 100.00 | 1122.9 |
| 293.15 | 100.00 | 1122.9 |
| 293.15 | 640.00 | 1123.1 |
| 293.15 | 1090.00 | 1123.4 |
| 293.15 | 1600.00 | 1123.6 |
| 293.15 | 2140.00 | 1123.8 |
| 293.15 | 3080.00 | 1124.2 |
| 293.15 | 5030.00 | 1125.1 |
| 293.15 | 7010.00 | 1125.9 |
| 293.15 | 9950.00 | 1127.2 |
| 293.15 | 14850.00 | 1129.3 |
| 293.15 | 19770.00 | 1131.3 |
| 293.15 | 24660.00 | 1133.3 |
| 293.15 | 29510.00 | 1135.2 |
| 293.15 | 34610.00 | 1137.2 |
| 293.15 | 39370.00 | 1139.1 |
| 293.15 | 44320.00 | 1141.0 |
| 293.15 | 49130.00 | 1142.8 |
| 293.15 | 54050.00 | 1144.6 |
| 293.15 | 59060.00 | 1146.4 |
| 293.15 | 63780.00 | 1148.0 |
| 303.15 | 100.00 | 1115.2 |
| 303.15 | 100.00 | 1115.1 |
| 303.15 | 630.00 | 1115.4 |
| 303.15 | 1130.00 | 1115.6 |
| 303.15 | 1620.00 | 1115.9 |
| 303.15 | 2140.00 | 1116.1 |
| 303.15 | 3070.00 | 1116.5 |
| 303.15 | 5080.00 | 1117.4 |
| 303.15 | 6960.00 | 1118.3 |
| 303.15 | 9960.00 | 1119.6 |
| 303.15 | 14840.00 | 1121.7 |
| 303.15 | 19750.00 | 1123.8 |
| 303.15 | 24670.00 | 1125.9 |
| 303.15 | 29570.00 | 1127.9 |
| 303.15 | 34500.00 | 1129.9 |
| 303.15 | 39360.00 | 1131.9 |
| 303.15 | 44300.00 | 1133.8 |
| 303.15 | 49190.00 | 1135.7 |
| 303.15 | 54090.00 | 1137.6 |
| 303.15 | 58850.00 | 1139.3 |
| 303.15 | 63890.00 | 1141.2 |
| 303.15 | 68750.00 | 1142.9 |
| 313.15 | 100.00 | 1107.4 |
| 313.15 | 100.00 | 1107.4 |
| 313.15 | 670.00 | 1107.6 |
| 313.15 | 1130.00 | 1107.9 |
| 313.15 | 1600.00 | 1108.1 |
| 313.15 | 2080.00 | 1108.3 |
| 313.15 | 3100.00 | 1108.8 |
| 313.15 | 5030.00 | 1109.7 |
| 313.15 | 7010.00 | 1110.6 |
| 313.15 | 10010.00 | 1112.0 |
| 313.15 | 14880.00 | 1114.2 |
| 313.15 | 19750.00 | 1116.4 |
| 313.15 | 24680.00 | 1118.6 |
| 313.15 | 29560.00 | 1120.6 |
| 313.15 | 34510.00 | 1122.7 |
| 313.15 | 39330.00 | 1124.7 |
| 313.15 | 44290.00 | 1126.7 |
| 313.15 | 49180.00 | 1128.6 |
| 313.15 | 54160.00 | 1130.6 |
| 313.15 | 59000.00 | 1132.4 |
| 313.15 | 63910.00 | 1134.3 |
| 313.15 | 68840.00 | 1136.0 |
| 323.15 | 100.00 | 1099.6 |
| 323.15 | 100.00 | 1099.5 |
| 323.15 | 590.00 | 1099.8 |
| 323.15 | 1140.00 | 1100.0 |
| 323.15 | 1600.00 | 1100.3 |
| 323.15 | 2080.00 | 1100.5 |
| 323.15 | 3020.00 | 1101.0 |
| 323.15 | 5050.00 | 1101.9 |
| 323.15 | 7000.00 | 1102.9 |
| 323.15 | 9970.00 | 1104.3 |
| 323.15 | 14870.00 | 1106.7 |
| 323.15 | 19780.00 | 1108.9 |
| 323.15 | 24700.00 | 1111.2 |
| 323.15 | 29650.00 | 1113.3 |
| 323.15 | 34470.00 | 1115.4 |
| 323.15 | 39340.00 | 1117.5 |
| 323.15 | 44250.00 | 1119.6 |
| 323.15 | 49170.00 | 1121.6 |
| 323.15 | 54080.00 | 1123.5 |
| 323.15 | 58970.00 | 1125.5 |
| 323.15 | 63800.00 | 1127.3 |
| 323.15 | 68780.00 | 1129.2 |
| 333.15 | 100.00 | 1091.7 |
| 333.15 | 100.00 | 1091.7 |
| 333.15 | 660.00 | 1092.0 |
| 333.15 | 1110.00 | 1092.2 |
| 333.15 | 1600.00 | 1092.5 |
| 333.15 | 2100.00 | 1092.7 |
| 333.15 | 3070.00 | 1093.2 |
| 333.15 | 5060.00 | 1094.2 |
| 333.15 | 6980.00 | 1095.2 |
| 333.15 | 9970.00 | 1096.6 |
| 333.15 | 14840.00 | 1099.0 |
| 333.15 | 19660.00 | 1101.3 |
| 333.15 | 24670.00 | 1103.7 |
| 333.15 | 29610.00 | 1106.0 |
| 333.15 | 34530.00 | 1108.2 |
| 333.15 | 39400.00 | 1110.3 |
| 333.15 | 44280.00 | 1112.5 |
| 333.15 | 49110.00 | 1114.5 |
| 333.15 | 54040.00 | 1116.5 |
| 333.15 | 59060.00 | 1118.6 |
| 333.15 | 63830.00 | 1120.5 |
| 333.15 | 68770.00 | 1122.4 |
| 343.15 | 100.00 | 1083.9 |
| 343.15 | 100.00 | 1083.9 |
| 343.15 | 640.00 | 1084.2 |
| 343.15 | 1120.00 | 1084.4 |
| 343.15 | 1600.00 | 1084.7 |
| 343.15 | 2110.00 | 1084.9 |
| 343.15 | 3040.00 | 1085.5 |
| 343.15 | 5040.00 | 1086.6 |
| 343.15 | 6960.00 | 1087.5 |
| 343.15 | 9920.00 | 1089.0 |
| 343.15 | 14810.00 | 1091.6 |
| 343.15 | 19680.00 | 1093.9 |
| 343.15 | 24620.00 | 1096.4 |
| 343.15 | 29580.00 | 1098.7 |
| 343.15 | 34460.00 | 1101.0 |
| 343.15 | 39370.00 | 1103.3 |
| 343.15 | 44240.00 | 1105.4 |
| 343.15 | 49160.00 | 1107.6 |
| 343.15 | 54020.00 | 1109.7 |
| 343.15 | 58940.00 | 1111.7 |
| 343.15 | 63890.00 | 1113.8 |
| 343.15 | 68680.00 | 1115.7 |
| 353.15 | 100.00 | 1076.0 |
| 353.15 | 100.00 | 1076.0 |
| 353.15 | 650.00 | 1076.3 |
| 353.15 | 1100.00 | 1076.5 |
| 353.15 | 1550.00 | 1076.7 |
| 353.15 | 2100.00 | 1077.1 |
| 353.15 | 3050.00 | 1077.6 |
| 353.15 | 5040.00 | 1078.6 |
| 353.15 | 7010.00 | 1079.8 |
| 353.15 | 9960.00 | 1081.3 |
| 353.15 | 14810.00 | 1084.0 |
| 353.15 | 19780.00 | 1086.5 |
| 353.15 | 24610.00 | 1089.0 |
| 353.15 | 29560.00 | 1091.9 |
| 353.15 | 34450.00 | 1093.8 |
| 353.15 | 39370.00 | 1096.1 |
| 353.15 | 44270.00 | 1098.4 |
| 353.15 | 49200.00 | 1100.6 |
| 353.15 | 54090.00 | 1102.8 |
| 353.15 | 59010.00 | 1104.9 |
| 353.15 | 63820.00 | 1107.0 |
| 353.15 | 68800.00 | 1109.0 |
| 363.15 | 100.00 | 1068.1 |
| 363.15 | 100.00 | 1068.0 |
| 363.15 | 660.00 | 1068.4 |
| 363.15 | 1120.00 | 1068.7 |
| 363.15 | 1560.00 | 1068.9 |
| 363.15 | 2130.00 | 1069.2 |
| 363.15 | 3050.00 | 1069.8 |
| 363.15 | 5090.00 | 1070.9 |
| 363.15 | 6990.00 | 1072.0 |
| 363.15 | 9980.00 | 1073.7 |
| 363.15 | 14880.00 | 1076.4 |
| 363.15 | 19680.00 | 1079.0 |
| 363.15 | 24720.00 | 1081.7 |
| 363.15 | 29630.00 | 1084.2 |
| 363.15 | 34490.00 | 1086.6 |
| 363.15 | 39430.00 | 1089.0 |
| 363.15 | 44200.00 | 1091.4 |
| 363.15 | 49240.00 | 1093.7 |
| 363.15 | 54100.00 | 1095.9 |
| 363.15 | 59010.00 | 1098.1 |
| 363.15 | 63880.00 | 1100.2 |
| 363.15 | 68830.00 | 1102.3 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [427.16; 586.55] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.94699e+01 | |||
| Coefficient B | -8.61684e+03 | |||
| Coefficient C | 2.20480e+01 | |||
| Temperature range, min. | 427.16 | |||
| Temperature range, max. | 586.55 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 450 500 550 | ||||
| Pvap | 1.33 | kPa | 427.16 | Calculated Property |
| Pvap | 2.76 | kPa | 444.87 | Calculated Property |
| Pvap | 5.42 | kPa | 462.58 | Calculated Property |
| Pvap | 10.14 | kPa | 480.29 | Calculated Property |
| Pvap | 18.18 | kPa | 498.00 | Calculated Property |
| Pvap | 31.38 | kPa | 515.71 | Calculated Property |
| Pvap | 52.31 | kPa | 533.42 | Calculated Property |
| Pvap | 84.47 | kPa | 551.13 | Calculated Property |
| Pvap | 132.56 | kPa | 568.84 | Calculated Property |
| Pvap | 202.63 | kPa | 586.55 | Calculated Property |
| Pvap | [5.30e-06; 3249.79] | kPa | [265.79; 700.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 2.93684e+01 | |||
| Coefficient B | -8.89710e+03 | |||
| Coefficient C | -1.46752e+00 | |||
| Coefficient D | 2.12637e-06 | |||
| Temperature range, min. | 265.79 | |||
| Temperature range, max. | 700.00 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 400 600 | ||||
| Pvap | 5.30e-06 | kPa | 265.79 | Calculated Property |
| Pvap | 7.53e-04 | kPa | 314.04 | Calculated Property |
| Pvap | 0.03 | kPa | 362.28 | Calculated Property |
| Pvap | 0.46 | kPa | 410.53 | Calculated Property |
| Pvap | 4.17 | kPa | 458.77 | Calculated Property |
| Pvap | 25.19 | kPa | 507.02 | Calculated Property |
| Pvap | 112.94 | kPa | 555.26 | Calculated Property |
| Pvap | 405.21 | kPa | 603.51 | Calculated Property |
| Pvap | 1226.12 | kPa | 651.75 | Calculated Property |
| Pvap | 3249.79 | kPa | 700.00 | Calculated Property |
Similar Compounds
![2-[2-[2-[2-[2-[2-[2-(2-Hydroxyethoxy)ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethanol.](data:image/png;base64,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)
![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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)
![2-[2-[2-[2-[2-[2-[2-[2-(2-Methoxyethoxy)ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethanol.](data:image/png;base64,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)
![Ethanol, 2-[2-(2-methoxyethoxy)ethoxy]-.](data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAPoAAAD6CAIAAAAHjs1qAAAMU0lEQVR4nO3cf0xV9R/H8fflh6KQXBnaZApJooWCFAKWNcls1cZam7JVA5fT0UzFyibNXHcLdS5/7P7hypv7LrH+EefmbtvXDFJMTZzfqSXDyQwzfhimXn8MkMu99/X949wABeEC91y++75fj7+6l8s9n3vv85zz+ZyLWQAIkQ5hIz0AotBh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qSImbm3tcmHH0p2tmRmypIl0txs4raoHwcPyksvSWam5ObKwYMjPZqRFGHic69bJz6fnDwpERGyc6fk58uJE2KxmLhF6u3XX+Xjj+XQIUlJkbo6ee01SUqSZ54Z6WGNDAsAU57Y45Hx4+XaNYmJ8d8za5Z8951kZJiyuUdra2v77bffkpOTJ06cGOJNd6mtrfV6vWlpaSOw7fffl9RUWbXKf3PnTqmpkV27Qj+Qmpoai8Uyc+bM0G+6i2mTmcZGiY/vbl1EZsyQK1fM2twjVFZWTpgw4bnnnktNTf366699Pl+IB3Dr1q01a9ZkZWWlp6dnZ2dfvXo1xAOQK1ckJaX75vTpof8UmpubFyxYkJaWlpOTs2TJkpaWlhAPoBtMcucOxo9/4J4FC3DsmFmb6+XixYuvv/668RrDw8ON/8jJyamurg7NANxu944dO6xWqzEAi8UiItHR0Rs3bmxvbw/NGADgnXewb1/3zX378PbbIdt4e3v7pk2bYmJiRMRisRgfRGxs7Pbt291ud8iG0cWE3I8cwdq1AJCZicpK/52NjUhIwJ07sNtRVgafL/jb/YfL5SopKRk9erSIWK3WzZs33717t7y8PDEx0XjT8/Pzr169at4AAFRUVHSdtRcuXHjhwoXLly8XFhYa0U+ePLmsrMxn5puA69exYgUuX8bu3cjP775/8WLs3o36eqxYgZYWEwcAOJ3O5ORk403Iy8urra2tq6vLz8837klJSSkvLzd1AL0FNff6eixaBBGIoKICp04hMRFr12LDBkybhr170dCAMWMggpwcmHCU9Xq9ZWVlxhw9LCyssLDwr7/+6vppa2urzWaLiooSkbFjx9psNjOOsv1/olVVVbNnzzZ+On/+/HPnzgV9AHC7sWMHrFaIYNEidHZi4ULk5WHjRuTl4ZVX0NmJ/HyIwGrF9u0w4ShbW1v76quvGi/zqaeeOnToUM+fVlRUzJo1q+exIOgDeJQg5d7aCpsNUVEQwdixsNlglHT7Nioq4HSiuRkAfD6UlyMxESKwWJCfjz/+CM4AgKNHjwZSUn19/aJFi4yHTZ069eCBA8EawF2X66OPPoqMjOz/fG3sk48//nif++RwVVRg5kz/EWfhQhgl+Xw4exb79+PsWf95ta7OX7wIUlIQvKPszZs3i4uLjUlLXFyc3W7v7Ozs/bCeM73IyMgPPvjgrssVrDH0Y9i59y54wHnCo/aNoWpoaBjsPKFr3/j3/PnIzcX588MZALxelJW1JiUlJiQEWPBDM64tW7bcv39/WGOoq0Ne3uAKrqjArFkP7xtD1dnZ6XA44uPjRSQiIqKoqOjvv//u/1e69o30iRO9iYmw2+HxDGcMAxpe7mfO4Pnn/e/XnDk4cWIQv/vnnygs9P/u5MlDm9D3np+0tbUF+Lsej+dfDof3iScggvBwvPcerl8f7AAAoKoKGRnGC/nx3XcHNT+5dOlSXl7ecOeyLhdKSjB6NEQQEwObDYHvOW43HA7Ex0MEkZEoKsJAjfap5/zk5ZdfHtT85Pz583VLl/pLmD0bR48OYQABGmLujY2NX6xahYgIiCAhAXv3DnH1eeQI0tONl7pt2bLzAR9lfT7fQ6vPP4Y2L+rZitWKLVsG0UpDAwoLYbEMZ49Fr3VtTU1NgL/o8XgcDsetF1/077FFRUPcY69fR1ERwsMhcuqFF3bt2uUJ+CgbtNWn04nkZH/0eXn4/fchPk+/Bp17R0eH3W5/7LHHROTCggVYvx737g1rCB4PvvrqP/PmhYWFGTOBloGuGJw5c2bevHnGW5yZmXliUGeVPl269MBM4PvvB3h87/lYwGeVPrndbrvd3jWXDWQmUFVVlZGRISLvzJjhy83F8Fe95855c3OzUlNF5Omnn/7hhx/6f/i9e/dsNpsxH4uJibHZbMOdj3V0wG7HuHEQwahRKC7GnTvDesJeBpf7Q5eWfg/eLhjgXLa5ubmoqCgsLExEJk2a5HA4vF5vsMbw8DrPOMq2t+PYMRw4gIsXgX/WKklJZqy2e6/z+jzKDmGtErhAPmJzV9tNTSgqQlgYRDBpEhwOGB/xxYs4cADHjnWv9H78EV2f/rVrgSzAAs2956WlQHb9oek5l50+ffr3PY6yxlll3LhxIjJq1Kji4uI7wd71AcDtht3uv4r35ZdobERKCpYvR2kpsrKwejW8XsyZAxFkZuL48eAPoN+32lirjBkzZghrlcD1PIH3fqurq6tzcnJM/9ruzBnMmwcRZGTA48Hq1cjORmkpli/HtGloaACAuDi0tvofv38/CgoGfNaBcw/wkBNEveey3377rUlnlb61tOCzz9DZiWXLsH27/063G6mpqK7GyZPYs8fUb8oAOJ3OqVOndr3k06dPl5eXJyUlDXetErCmpqauE2lCQoLD4Th79mxIvynz+VBWhhMncPo0UlPRdUFz61YsXQqYkHtHR8eUKVOMCeWaNWtu3bo1jOEPQkdHx7Zt22JjY43TpfGpp6en//TTT6EZgN+TTz4wVykpwRdfhGzjbW1tpaWl0dHR0kNWVtYvv/wSsjGcOnUqOzu75wCio6M///xzM84qj7R1Kz75pPtmfT2SkwEgLg5OJw4fxuHD2LAhOEf3zZs3D/bSUrDcuHFj1apV0dHR4eHh69at6/MLC3NNmPDAhblNm/DppyEeQlNT07PPPmucWoO8VgmMcRHMuKCekpJi9lmlDxs2oLS0++aNG4iPB4C4OKxdi5ISlJTgzTeDk3vo39+H3L59O6THkp7mzn3gy4SCAuzZMyIDcblcIf3Dsl7a29tdIfnisw/ffPNAysePY+5cYCiTmYH/ALhrLjFSYmNjjcXZCFi5Utavl5s3RUQqK+X4cfnnDxBCzGq1Gt+mjZSoqCjjOukIWLxYfv5ZKitFRG7elPXrZeXKoT2Tmf+a6f9AQYG4XPLGG3L/vkyZIk7nA3/BT6EREyNOp9hsUlIiUVHy1ltSUCAikpYmXcdiq1WSkgZ8JtP+NRPR/x7+nwhIEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOivwXOGiJ/kNK0vYAAAAASUVORK5CYII=)
![2-[2-[2-[2-[2-[2-[2-[2-[2-[2-(2-Methoxyethoxy)ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethanol.](data:image/png;base64,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)
![2-[2-[2-[2-[2-[2-[2-(2-Methoxyethoxy)ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethanol.](data:image/png;base64,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)
Find more compounds similar to Triethylene glycol.
Mixtures
- Benzene, chloro- + Triethylene glycol
- Benzene, bromo- + Triethylene glycol
- Benzene, nitro- + Triethylene glycol
- Triethylene glycol + Thiophene, tetrahydro-, 1,1-dioxide
- Triethylene glycol + Water
- 1,2-Ethanediol + Triethylene glycol
- Triethylene glycol + Ethanol, 2,2'-oxybis-
- 1,2-Ethanediol + Triethylene glycol + Ethanol, 2,2'-oxybis-
- Toluene + Decane + Triethylene glycol
- Triethylene glycol + lithium chloride + Water
- lithium bromide + Triethylene glycol + Water
- Triethylene glycol + Tromethamine + Water
- Triethylene glycol + Pentane
- n-Hexane + Triethylene glycol
- Triethylene glycol + Heptane
- Octane + Triethylene glycol
- Triethylene glycol + Nonane
- Triethylene glycol + 1-Pentene
- 1-Hexene + Triethylene glycol
- 1-Heptene + Triethylene glycol
Find more mixtures with Triethylene glycol.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Application of the Multi-Current Transient Hot-Wire Technique for Absolute Measurements of the Thermal Conductivity of Glycols
- Thermophysical Properties For Diethylene Glycol + Nitrobenzene and Triethylene Glycol + (Chloro-, Bromo-, Nitro-) Benzene Systems at Different Temperatures
- Measurement of the triethylene glycol solubility in supercritical methane at pressures up to 9MPa
- Mutual diffusion coefficients of aqueous solutions of some glycols
- Liquid-liquid equilibrium in the ternary systems triethylene glycol + salts + water at different temperatures; experiment and correlation
- Temperature change from isenthalpic expansion of aqueous triethylene glycol mixtures for natural gas dehydration
- Experimental study of the density and viscosity of polyethylene glycols and their mixtures at temperatures from 293 K to 465 K and at high pressures up to 245 MPa
- Experimental study and phase equilibrium modeling of systems containing acid gas and glycol
- Prediction of refractive index and density of deep eutectic solvents using atomic contributions
- Removal of aromatic hydrocarbons from hydrocarbon mixture using glycols at 303.15 K and 333.15 K and atmospheric pressure: Experimental and calculated data by NRTL and UNIQUAC models
- Liquid-liquid phase diagrams of poly(ethylene glycol) and aromatic hydrocarbons
- Carbon dioxide solubility in triethylene glycol and aqueous solutions
- New measurements and modeling of high pressure thermodynamic properties of glycols
- Critical temperatures and pressures of ethylene glycols
- Viscosity of liquid diethylene, triethylene and tetraethylene glycols at moderately high pressures using a vibrating wire instrument
- Separation of thiophene, or benzothiophene from model fuel using glycols. Liquid-liquid phase equilibria and oxidative desulfurization study
- Effective extraction of benzene and thiophene by novel deep eutectic solvents from hexane / aromatic mixture at different temperatures
- The experimental study on the influence of crown ethers and glycols on the mutual solubility of lithium bromide in water
- Vapour pressures, densities, and viscosities of the aqueous solutions containing (triethylene glycol or propylene glycol) and (LiCl or LiBr)
- Densities and vapor pressures of mixed-solvent desiccant systems containing {glycol (diethylene, or triethylene, or tetraethylene glycol) + salt (magnesium chloride) + water}
- Experimental and predicted refractive index properties in ternary mixtures of associated liquids
- Experimental study of the density and viscosity of polyethylene glycols and their mixtures at temperatures from 293 K to 473 K and at atmospheric pressure
- Molar heat capacities of some aqueous 2-amino-2-hydroxymethyl-1,3-propanediol + glycol systems
- Thermophysical property characterization of ternary system containing {glycol (DEG/TEG/T4EG) + 2-amino-2-hydroxymethyl-1,3-propanediol + water}
- Activity coefficients at infinite dilution of organic solutes in diethylene glycol and triethylene glycol from gas-liquid chromatography
- Isobaric specific heat capacity of typical lithium chloride liquid desiccants using scanning calorimetry
- Solubilities and thermodynamic properties of CO2 in choline-chloride based deep eutectic solvents
- Density and vapour pressure of mixed-solvent desiccant systems (propylene glycol or dipropylene glycol or tripropylene glycol + magnesium chloride + water)
- Acoustic and volumetric studies on (triethylene glycol + water) mixtures in a wide temperature range
- Measurement and correlation of physicochemical properties of phosphonium-based deep eutectic solvents at several temperatures (293.15 K - 343.15 K) for CO2 capture
- Thermal stability analysis, experimental conductivity and pH of phosphonium-based deep eutectic solvents and their prediction by a new empirical equation
- Thermodynamics properties of binary mixtures of aqueous solutions of glycols at several temperatures and atmospheric pressure
- Phase equilibria study on bromide-based ionic liquids with glycols and sulfolane. Experimental data and correlation
- Volumetric and ultrasonic studies on interactions of ethylene glycol, diethylene glycol and triethylene glycol in aqueous solutions of glycerol at temperatures T = (293.15 K - 308.15) K
- Acoustic and thermodynamic study of D-Panthenol in aqueous solutions of glycol at different temperatures
- Excess molar enthalpies of binary mixtures containing ethylene glycols or poly(ethylene glycols) + ethyl alcohol at 308.15K and atmospheric pressure
- Heat capacities of the mixed-solvents desiccants (glycols +water + salts)
- Experimental and predicted excess molar enthalpies of some working pairs for absorption cycles
- Heat Capacity of Several Mixed-Solvent Desiccants Containing Glycol + Water + MgCl2
- Molar heat capacity of several aqueous solutions of n-[tris(hydroxymethyl)methyl-3-amino]- propanesulfonic acid (TAPS) + glycol
- Density of aqueous choline chloride-based ionic liquids analogues
- Experimental and prediction of volumetric properties of aqueous solution of (allyltriphenylPhosphonium bromide - Triethylene glycol) deep eutectic solvents
- Partial Molar Volumes and Partial Molar Isentropic Compressions of Four Poly(Ethylene Glycols) at Infinite Dilution in Water at Temperatures T = (278 to 343) K and Atmospheric Pressure
- Thermophysical properties of glycols and glymes
- Solubility and Spectral Studies for SO2 in Binary System of Tri-ethylene Glycol + Dimethyl Sulfoxide at T = (298.15, 303.15, and 308.15) K and p = 123.15 kPa
- Molar Heat Capacity of Selected Type III Deep Eutectic Solvents
- Investigation on Temperature-Dependent Volumetric and Acoustical Properties of Homologous Series of Glycols in Aqueous Sorbitol Solutions
- Measurement and Modeling of Isobaric Vapor-Liquid Equilibrium of Water + Glycols
- Thermodynamic Interactions Study of Some Ethylene Glycols in Aqueous Aniline Solutions at Different Temperatures: An Acoustical and Volumetric Approach
- Effect of Ethylene, Diethylene, and Triethylene Glycols and Glycerol on the Physicochemical Properties and Phase Behavior of Benzyltrimethyl and Benzyltributylammonium Chloride Based Deep Eutectic Solvents at 283.15-343.15 K
- Vapor-Liquid Phase Equilibrium for Separation of Isopropanol from Its Aqueous Solution by Choline Chloride-Based Deep Eutectic Solvent Selected by COSMO-SAC Model
- Liquid-Liquid Equilibria for Benzene/Thiophene + Cyclohexane/Hexadecane + Deep Eutectic Solvents: Data and Correlation
- Densities, Viscosities, and Excess Properties for Binary Mixtures of Some Glycols and Polyglycols in N-Methylacetamide at 308.15 K
- Infinite Dilution Activity Coefficients of Hydrocarbons in Triethylene Glycol and Tetraethylene Glycol
- Density, Viscosity and Thermal Conductivity of Aqueous Ethylene, Diethylene and Triethylene Glycol Mixtures between 290 K and 450 K
- Excess Molar Enthalpies of Binary Mixtures Containing Glycols or Polyglycols + Dimethyl Sulfoxide at 308.15 K
- Densities, Excess Molar Volumes, Viscosities, Speeds of Sound, Excess Isentropic Compressibilities, and Relative Permittivities for Alkyl (Methyl, Ethyl, Butyl, and Isoamyl) Acetates + Glycols at Different Temperatures
- Thermodynamic Study of Binary Mixtures Containing Glycols or Polyethylene Glycols + Benzyl Alcohol at 308.15 K
- Excess Molar Enthalpies and Hydrogen Bonding in Binary Mixtures Containing Glycols or Poly(Ethylene Glycols) and 2-Phenylethyl Alcohol at 308.15 K and Atmospheric Pressure
- Excess Molar Enthalpies and Hydrogen Bonding in Binary Mixtures Containing Ethers and Benzyl Alcohol at 308.15 K and Atmospheric Pressure
- Liquid-Liquid Equilibria for Binary and Ternary Systems Containing Glycols, Aromatic Hydrocarbons, and Water: Experimental Measurements and Modeling with the CPA EoS
- Heat Capacities of Four Promising Alternatives to Lithium Bromide Aqueous Solution in Absorption Refrigerators
- Isobaric Vapor-Liquid Equilibrium for Four Binary Systems of Ethane-1,2-diol, Butane-1,4-diol, 2-(2- Hydroxyethoxy)ethan-1-ol and 2-[2-(2- Hydroxyethoxy)ethoxy]ethanol at 10.0 kPa, 20.0 kPa and 40.0 kPa
- Solubility of CO2 in Nonaqueous Absorption System of 2-(2-Aminoethylamine)ethanol + Benzyl Alcohol
- Density, Viscosities, and Excess Properties for Binary Mixtures of Sulfolane + Alcohols and Sulfolane + Glycols at Different Temperatures
- Tetrabutylammonium Chloride Based Ionic Liquid Analogues and Their Physical Properties
- Liquid-Liquid Equilibria of (Limonene + Linalool + Ethylene Glycol or Diethylene Glycol or Triethylene Glycol or 1,2-Propylene Glycol) Ternary Systems
- Vapor-Liquid Equilibria of Water + Triethylene Glycol (TEG) and Water + TEG + Toluene at 85 kPa
- Measurement and Correlation for Solubility of Thiourea in Triglycol + Water at Temperatures from (292.05 to 357.75) K
- Measurement and Correlation of Densities and Viscosities of Thiourea in Triglycol + Water at Temperatures from (302.85 to 341.45) K
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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