- InChI
- InChI=1S/C8H18O5/c9-1-3-11-5-7-13-8-6-12-4-2-10/h9-10H,1-8H2
- InChI Key
- UWHCKJMYHZGTIT-UHFFFAOYSA-N
- Formula
- C8H18O5
- SMILES
- OCCOCCOCCOCCO
- Molecular Weight1
- 194.23
- CAS
- 112-60-7
- Other Names
-
- 1,11-Dihydroxy-3,6,9-trioxaundecane
- 1,11-undecanediol, 3,6,9-trioxa-
- 2,2'-(Oxybis(ethyleneoxy))diethanol
- 2-(2-[2-(2-Hydroxyethoxy)ethoxy]ethoxy)ethanol
- 3,6,9-Trioxaundecan-1,11-diol
- 3,6,9-Trioxaundecane-1,11-diol
- 3,6,9-trioxa-1,11-undecanediol
- Ethanol, 2,2'-(oxybis(ethyleneoxy))di-
- Ethanol, 2,2'-[oxybis(2,1-ethanediyloxy)]bis-
- Hi-Dry
- NSC 1262
- PEG-4
- Tetraglycol
- ethanol, 2,2'-[oxybis(2,1-ethanediyloxy)]-
- 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).
- 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 | -4738.80 ± 4.60 | kJ/mol | NIST |
| ΔfG° | -572.16 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -909.57 | kJ/mol | Joback Calculated Property |
| ΔfH°liquid | -981.70 ± 4.60 | kJ/mol | NIST |
| ΔfusH° | 28.22 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 73.99 | kJ/mol | Joback Calculated Property |
| log10WS | 1.04 | Crippen Calculated Property | |
| logPoct/wat | -0.979 | Crippen Calculated Property | |
| McVol | 152.930 | ml/mol | McGowan Calculated Property |
| Pc | 3200.00 ± 100.00 | kPa | NIST |
| Inp | [1507.00; 1515.40] |
|
|
| Inp | 1507.00 | NIST | |
| Inp | 1515.40 | NIST | |
| Inp | 1515.40 | NIST | |
| Tboil | [587.20; 601.20] | K |
|
| Tboil | 587.20 | K | NIST |
| Tboil | 601.20 | K | NIST |
| Tc | [762.00; 814.00] | K |
|
| Tc | 814.00 | K | Critica... |
| Tc | 800.00 ± 30.00 | K | NIST |
| Tc | 762.00 ± 20.00 | K | NIST |
| Tfus | [263.75; 269.05] | K |
|
| Tfus | 269.05 | K | NIST |
| Tfus | 263.75 ± 0.70 | K | NIST |
| Vc | 0.576 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [418.43; 474.22] | J/mol×K | [634.06; 793.37] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 420 430 440 450 460 470 650 700 750 | ||||
| Cp,gas | 418.43 | J/mol×K | 634.06 | Joback Calculated Property |
| Cp,gas | 428.67 | J/mol×K | 660.61 | Joback Calculated Property |
| Cp,gas | 438.54 | J/mol×K | 687.16 | Joback Calculated Property |
| Cp,gas | 448.03 | J/mol×K | 713.72 | Joback Calculated Property |
| Cp,gas | 457.15 | J/mol×K | 740.27 | Joback Calculated Property |
| Cp,gas | 465.88 | J/mol×K | 766.82 | Joback Calculated Property |
| Cp,gas | 474.22 | J/mol×K | 793.37 | Joback Calculated Property |
| Cp,liquid | [419.20; 449.10] | J/mol×K | [298.00; 353.15] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 420 425 430 435 440 445 450 300 320 340 | ||||
| Cp,liquid | 428.80 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 419.20 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 428.50 | J/mol×K | 303.15 | Heat ca... |
| Cp,liquid | 430.90 | J/mol×K | 313.15 | Heat ca... |
| Cp,liquid | 434.70 | J/mol×K | 323.15 | Heat ca... |
| Cp,liquid | 438.50 | J/mol×K | 333.15 | Heat ca... |
| Cp,liquid | 443.60 | J/mol×K | 343.15 | Heat ca... |
| Cp,liquid | 449.10 | J/mol×K | 353.15 | Heat ca... |
| η | [0.0000148; 0.0037933] | Pa×s | [368.25; 634.06] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 5.00e-4 1.00e-3 1.50e-3 2.00e-3 2.50e-3 3.00e-3 3.50e-3 4.00e-3 400 500 600 | ||||
| η | 0.0037933 | Pa×s | 368.25 | Joback Calculated Property |
| η | 0.0009170 | Pa×s | 412.55 | Joback Calculated Property |
| η | 0.0002920 | Pa×s | 456.85 | Joback Calculated Property |
| η | 0.0001138 | Pa×s | 501.15 | Joback Calculated Property |
| η | 0.0000517 | Pa×s | 545.46 | Joback Calculated Property |
| η | 0.0000264 | Pa×s | 589.76 | Joback Calculated Property |
| η | 0.0000148 | Pa×s | 634.06 | Joback Calculated Property |
| ΔvapH | [92.20; 99.00] | kJ/mol | [273.00; 503.50] |
|
| ΔvapH | 99.00 ± 10.00 | kJ/mol | 273.00 | NIST |
| ΔvapH | 92.20 | kJ/mol | 503.50 | NIST |
| n0 | 1.45710 | 293.15 | Infinit... | |
| ρl | [1063.20; 1135.81] | kg/m3 | [278.15; 373.15] |
|
|
T(K) Liquid Density (kg/m3) 1060 1080 1100 1120 1140 300 350 | ||||
| ρl | 1135.81 | kg/m3 | 278.15 | Volumet... |
| ρl | 1131.85 | kg/m3 | 283.15 | Volumet... |
| ρl | 1132.10 | kg/m3 | 283.15 | Thermop... |
| ρl | 1127.88 | kg/m3 | 288.15 | Volumet... |
| ρl | 1131.20 | kg/m3 | 288.15 | Thermop... |
| ρl | 1128.10 | kg/m3 | 288.15 | Thermop... |
| ρl | 1123.90 | kg/m3 | 293.15 | Volumet... |
| ρl | 1127.10 | kg/m3 | 293.15 | Thermop... |
| ρl | 1124.10 | kg/m3 | 293.15 | Thermop... |
| ρl | 1120.10 | kg/m3 | 298.15 | Thermop... |
| ρl | 1123.10 | kg/m3 | 298.15 | Thermop... |
| ρl | 1120.09 | kg/m3 | 298.15 | Excess ... |
| ρl | 1120.09 | kg/m3 | 298.15 | Thermod... |
| ρl | 1119.92 | kg/m3 | 298.15 | Volumet... |
| ρl | 1116.10 | kg/m3 | 303.15 | Thermop... |
| ρl | 1119.10 | kg/m3 | 303.15 | Thermop... |
| ρl | 1116.00 | kg/m3 | 303.15 | Vapour ... |
| ρl | 1115.94 | kg/m3 | 303.15 | Volumet... |
| ρl | 1112.28 | kg/m3 | 308.15 | Excess ... |
| ρl | 1112.31 | kg/m3 | 308.15 | Thermod... |
| ρl | 1111.96 | kg/m3 | 308.15 | Volumet... |
| ρl | 1112.20 | kg/m3 | 308.15 | Thermop... |
| ρl | 1115.10 | kg/m3 | 308.15 | Thermop... |
| ρl | 1112.28 | kg/m3 | 308.15 | Excess ... |
| ρl | 1112.32 | kg/m3 | 308.50 | Excess ... |
| ρl | 1111.10 | kg/m3 | 313.15 | Thermop... |
| ρl | 1108.00 | kg/m3 | 313.15 | Vapour ... |
| ρl | 1107.98 | kg/m3 | 313.15 | Volumet... |
| ρl | 1108.20 | kg/m3 | 313.15 | Thermop... |
| ρl | 1107.20 | kg/m3 | 318.15 | Thermop... |
| ρl | 1104.01 | kg/m3 | 318.15 | Volumet... |
| ρl | 1100.20 | kg/m3 | 323.15 | Thermop... |
| ρl | 1100.02 | kg/m3 | 323.15 | Volumet... |
| ρl | 1100.00 | kg/m3 | 323.15 | Vapour ... |
| ρl | 1103.20 | kg/m3 | 323.15 | Thermop... |
| ρl | 1099.20 | kg/m3 | 328.15 | Thermop... |
| ρl | 1096.04 | kg/m3 | 328.15 | Volumet... |
| ρl | 1092.05 | kg/m3 | 333.15 | Volumet... |
| ρl | 1095.30 | kg/m3 | 333.15 | Thermop... |
| ρl | 1093.00 | kg/m3 | 333.15 | Vapour ... |
| ρl | 1092.20 | kg/m3 | 333.15 | Thermop... |
| ρl | 1091.30 | kg/m3 | 338.15 | Thermop... |
| ρl | 1086.00 | kg/m3 | 343.15 | Vapour ... |
| ρl | 1084.30 | kg/m3 | 343.15 | Thermop... |
| ρl | 1087.30 | kg/m3 | 343.15 | Thermop... |
| ρl | 1083.40 | kg/m3 | 348.15 | Thermop... |
| ρl | 1079.40 | kg/m3 | 353.15 | Thermop... |
| ρl | 1075.30 | kg/m3 | 358.15 | Thermop... |
| ρl | 1071.30 | kg/m3 | 363.15 | Thermop... |
| ρl | 1067.30 | kg/m3 | 368.15 | Thermop... |
| ρl | 1063.20 | kg/m3 | 373.15 | Thermop... |
| λ | [0.18; 0.19] | W/m×K | [298.20; 338.20] |
|
|
T(K) Liquid thermal conductivity (W/m×K) 0.19 0.19 0.19 0.19 0.19 0.19 300 310 320 330 | ||||
| λ | 0.18 | W/m×K | 298.20 | Applica... |
| λ | 0.19 | W/m×K | 308.20 | Applica... |
| λ | 0.19 | W/m×K | 318.30 | Applica... |
| λ | 0.19 | W/m×K | 328.20 | Applica... |
| λ | 0.19 | W/m×K | 338.20 | Applica... |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 283.13 | 100.00 | 1132.0 |
| 283.13 | 1000.00 | 1132.4 |
| 283.13 | 2000.00 | 1132.8 |
| 283.13 | 5000.00 | 1134.1 |
| 283.13 | 7000.00 | 1135.0 |
| 283.13 | 10000.00 | 1136.4 |
| 283.13 | 12000.00 | 1137.2 |
| 283.13 | 16000.00 | 1138.9 |
| 283.13 | 20000.00 | 1140.6 |
| 283.13 | 25000.00 | 1142.8 |
| 283.13 | 30000.00 | 1144.8 |
| 283.13 | 35000.00 | 1146.9 |
| 283.13 | 40000.00 | 1148.8 |
| 283.13 | 45000.00 | 1150.7 |
| 283.13 | 50000.00 | 1152.6 |
| 283.13 | 55000.00 | 1154.5 |
| 283.13 | 60000.00 | 1156.3 |
| 283.13 | 65000.00 | 1158.2 |
| 283.13 | 70000.00 | 1159.9 |
| 283.13 | 75000.00 | 1161.7 |
| 283.13 | 80000.00 | 1163.3 |
| 283.13 | 85000.00 | 1165.1 |
| 283.13 | 90000.00 | 1166.7 |
| 283.13 | 95000.00 | 1168.4 |
| 293.11 | 100.00 | 1123.8 |
| 293.11 | 1000.00 | 1124.2 |
| 293.11 | 2000.00 | 1124.7 |
| 293.11 | 5000.00 | 1126.1 |
| 293.11 | 7000.00 | 1127.0 |
| 293.11 | 10000.00 | 1128.4 |
| 293.11 | 12000.00 | 1129.2 |
| 293.11 | 16000.00 | 1131.1 |
| 293.11 | 20000.00 | 1132.8 |
| 293.11 | 25000.00 | 1134.9 |
| 293.11 | 30000.00 | 1137.1 |
| 293.11 | 35000.00 | 1139.0 |
| 293.11 | 40000.00 | 1141.1 |
| 293.11 | 45000.00 | 1143.1 |
| 293.11 | 50000.00 | 1145.1 |
| 293.11 | 55000.00 | 1147.0 |
| 293.11 | 60000.00 | 1148.9 |
| 293.11 | 65000.00 | 1150.8 |
| 293.11 | 70000.00 | 1152.6 |
| 293.11 | 75000.00 | 1154.4 |
| 293.11 | 80000.00 | 1156.2 |
| 293.11 | 85000.00 | 1157.9 |
| 293.11 | 90000.00 | 1159.6 |
| 293.11 | 95000.00 | 1161.3 |
| 303.13 | 100.00 | 1115.8 |
| 303.13 | 1000.00 | 1116.1 |
| 303.13 | 2000.00 | 1116.7 |
| 303.13 | 5000.00 | 1118.1 |
| 303.13 | 7000.00 | 1119.1 |
| 303.13 | 10000.00 | 1120.5 |
| 303.13 | 12000.00 | 1121.4 |
| 303.13 | 16000.00 | 1123.3 |
| 303.13 | 20000.00 | 1125.0 |
| 303.13 | 25000.00 | 1127.3 |
| 303.13 | 30000.00 | 1129.5 |
| 303.13 | 35000.00 | 1131.6 |
| 303.13 | 40000.00 | 1133.7 |
| 303.13 | 45000.00 | 1135.7 |
| 303.13 | 50000.00 | 1137.7 |
| 303.13 | 55000.00 | 1139.7 |
| 303.13 | 60000.00 | 1141.7 |
| 303.13 | 65000.00 | 1143.6 |
| 303.13 | 70000.00 | 1145.5 |
| 303.13 | 75000.00 | 1147.4 |
| 303.13 | 80000.00 | 1149.1 |
| 303.13 | 85000.00 | 1150.8 |
| 303.13 | 90000.00 | 1152.6 |
| 303.13 | 95000.00 | 1154.4 |
| 313.22 | 100.00 | 1107.8 |
| 313.22 | 1000.00 | 1108.1 |
| 313.22 | 2000.00 | 1108.6 |
| 313.22 | 5000.00 | 1110.1 |
| 313.22 | 7000.00 | 1111.1 |
| 313.22 | 10000.00 | 1112.6 |
| 313.22 | 12000.00 | 1113.6 |
| 313.22 | 16000.00 | 1115.5 |
| 313.22 | 20000.00 | 1117.3 |
| 313.22 | 25000.00 | 1119.7 |
| 313.22 | 30000.00 | 1121.9 |
| 313.22 | 35000.00 | 1124.1 |
| 313.22 | 40000.00 | 1126.3 |
| 313.22 | 45000.00 | 1128.4 |
| 313.22 | 50000.00 | 1130.4 |
| 313.22 | 55000.00 | 1132.5 |
| 313.22 | 60000.00 | 1134.5 |
| 313.22 | 65000.00 | 1136.5 |
| 313.22 | 70000.00 | 1138.4 |
| 313.22 | 75000.00 | 1140.3 |
| 313.22 | 80000.00 | 1142.2 |
| 313.22 | 85000.00 | 1144.0 |
| 313.22 | 90000.00 | 1145.8 |
| 313.22 | 95000.00 | 1147.7 |
| 323.20 | 100.00 | 1099.8 |
| 323.20 | 1000.00 | 1100.1 |
| 323.20 | 2000.00 | 1100.6 |
| 323.20 | 5000.00 | 1102.2 |
| 323.20 | 7000.00 | 1103.2 |
| 323.20 | 10000.00 | 1104.7 |
| 323.20 | 12000.00 | 1105.6 |
| 323.20 | 16000.00 | 1107.7 |
| 323.20 | 20000.00 | 1109.6 |
| 323.20 | 25000.00 | 1111.9 |
| 323.20 | 30000.00 | 1114.3 |
| 323.20 | 35000.00 | 1116.6 |
| 323.20 | 40000.00 | 1118.8 |
| 323.20 | 45000.00 | 1121.0 |
| 323.20 | 50000.00 | 1123.2 |
| 323.20 | 55000.00 | 1125.5 |
| 323.20 | 60000.00 | 1127.4 |
| 323.20 | 65000.00 | 1129.4 |
| 323.20 | 70000.00 | 1131.3 |
| 323.20 | 75000.00 | 1133.3 |
| 323.20 | 80000.00 | 1135.2 |
| 323.20 | 85000.00 | 1137.1 |
| 323.20 | 90000.00 | 1139.0 |
| 323.20 | 95000.00 | 1140.7 |
| 333.20 | 100.00 | 1091.8 |
| 333.20 | 1000.00 | 1092.3 |
| 333.20 | 2000.00 | 1092.9 |
| 333.20 | 5000.00 | 1094.5 |
| 333.20 | 7000.00 | 1095.6 |
| 333.20 | 10000.00 | 1097.1 |
| 333.20 | 12000.00 | 1098.1 |
| 333.20 | 16000.00 | 1100.2 |
| 333.20 | 20000.00 | 1102.2 |
| 333.20 | 25000.00 | 1104.6 |
| 333.20 | 30000.00 | 1107.1 |
| 333.20 | 35000.00 | 1109.4 |
| 333.20 | 40000.00 | 1111.7 |
| 333.20 | 45000.00 | 1113.9 |
| 333.20 | 50000.00 | 1116.2 |
| 333.20 | 55000.00 | 1118.4 |
| 333.20 | 60000.00 | 1120.5 |
| 333.20 | 65000.00 | 1122.5 |
| 333.20 | 70000.00 | 1124.6 |
| 333.20 | 75000.00 | 1126.6 |
| 333.20 | 80000.00 | 1128.5 |
| 333.20 | 85000.00 | 1130.4 |
| 333.20 | 90000.00 | 1132.2 |
| 333.20 | 95000.00 | 1134.1 |
| 343.17 | 100.00 | 1084.0 |
| 343.17 | 1000.00 | 1084.4 |
| 343.17 | 2000.00 | 1085.0 |
| 343.17 | 5000.00 | 1086.7 |
| 343.17 | 7000.00 | 1087.7 |
| 343.17 | 10000.00 | 1089.4 |
| 343.17 | 12000.00 | 1090.4 |
| 343.17 | 16000.00 | 1092.5 |
| 343.17 | 20000.00 | 1094.6 |
| 343.17 | 25000.00 | 1097.1 |
| 343.17 | 30000.00 | 1099.7 |
| 343.17 | 35000.00 | 1102.1 |
| 343.17 | 40000.00 | 1104.5 |
| 343.17 | 45000.00 | 1106.8 |
| 343.17 | 50000.00 | 1109.1 |
| 343.17 | 55000.00 | 1111.3 |
| 343.17 | 60000.00 | 1113.5 |
| 343.17 | 65000.00 | 1115.7 |
| 343.17 | 70000.00 | 1117.7 |
| 343.17 | 75000.00 | 1119.8 |
| 343.17 | 80000.00 | 1121.9 |
| 343.17 | 85000.00 | 1123.8 |
| 343.17 | 90000.00 | 1125.8 |
| 343.17 | 95000.00 | 1127.6 |
| 353.13 | 100.00 | 1075.9 |
| 353.13 | 1000.00 | 1076.4 |
| 353.13 | 2000.00 | 1076.9 |
| 353.13 | 5000.00 | 1078.7 |
| 353.13 | 7000.00 | 1079.9 |
| 353.13 | 10000.00 | 1081.6 |
| 353.13 | 12000.00 | 1082.8 |
| 353.13 | 16000.00 | 1084.9 |
| 353.13 | 20000.00 | 1087.1 |
| 353.13 | 25000.00 | 1089.8 |
| 353.13 | 30000.00 | 1092.3 |
| 353.13 | 35000.00 | 1094.9 |
| 353.13 | 40000.00 | 1097.3 |
| 353.13 | 45000.00 | 1099.8 |
| 353.13 | 50000.00 | 1102.1 |
| 353.13 | 55000.00 | 1104.3 |
| 353.13 | 60000.00 | 1106.6 |
| 353.13 | 65000.00 | 1108.9 |
| 353.13 | 70000.00 | 1111.0 |
| 353.13 | 75000.00 | 1113.2 |
| 353.13 | 80000.00 | 1115.2 |
| 353.13 | 85000.00 | 1117.2 |
| 353.13 | 90000.00 | 1119.2 |
| 353.13 | 95000.00 | 1121.1 |
| 363.20 | 100.00 | 1067.8 |
| 363.20 | 1000.00 | 1068.4 |
| 363.20 | 2000.00 | 1069.0 |
| 363.20 | 5000.00 | 1070.8 |
| 363.20 | 7000.00 | 1072.0 |
| 363.20 | 10000.00 | 1073.7 |
| 363.20 | 12000.00 | 1074.9 |
| 363.20 | 16000.00 | 1077.1 |
| 363.20 | 20000.00 | 1079.5 |
| 363.20 | 25000.00 | 1082.3 |
| 363.20 | 30000.00 | 1084.8 |
| 363.20 | 35000.00 | 1087.5 |
| 363.20 | 40000.00 | 1089.9 |
| 363.20 | 45000.00 | 1092.4 |
| 363.20 | 50000.00 | 1094.8 |
| 363.20 | 55000.00 | 1097.2 |
| 363.20 | 60000.00 | 1099.5 |
| 363.20 | 65000.00 | 1101.8 |
| 363.20 | 70000.00 | 1104.0 |
| 363.20 | 75000.00 | 1106.2 |
| 363.20 | 80000.00 | 1108.4 |
| 363.20 | 85000.00 | 1110.4 |
| 363.20 | 90000.00 | 1112.5 |
| 363.20 | 95000.00 | 1114.4 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 283.15 | 100.00 | 1130.1 |
| 283.15 | 100.00 | 1130.1 |
| 283.15 | 630.00 | 1130.3 |
| 283.15 | 1170.00 | 1130.2 |
| 283.15 | 1640.00 | 1130.8 |
| 283.15 | 2110.00 | 1131.0 |
| 283.15 | 3060.00 | 1131.4 |
| 283.15 | 5060.00 | 1132.2 |
| 283.15 | 7000.00 | 1133.1 |
| 283.15 | 9990.00 | 1134.3 |
| 283.15 | 14800.00 | 1136.3 |
| 283.15 | 19770.00 | 1138.4 |
| 283.15 | 24630.00 | 1140.4 |
| 283.15 | 29550.00 | 1142.3 |
| 283.15 | 34530.00 | 1144.2 |
| 283.15 | 39370.00 | 1146.1 |
| 283.15 | 44340.00 | 1147.9 |
| 283.15 | 49210.00 | 1149.7 |
| 283.15 | 54130.00 | 1151.5 |
| 283.15 | 59040.00 | 1153.3 |
| 283.15 | 63940.00 | 1155.0 |
| 283.15 | 68790.00 | 1156.7 |
| 293.15 | 100.00 | 1122.0 |
| 293.15 | 100.00 | 1122.0 |
| 293.15 | 570.00 | 1122.2 |
| 293.15 | 1090.00 | 1122.4 |
| 293.15 | 1480.00 | 1122.6 |
| 293.15 | 2030.00 | 1122.8 |
| 293.15 | 3030.00 | 1123.3 |
| 293.15 | 5050.00 | 1124.2 |
| 293.15 | 7090.00 | 1125.1 |
| 293.15 | 9890.00 | 1126.3 |
| 293.15 | 14910.00 | 1128.5 |
| 293.15 | 19720.00 | 1130.5 |
| 293.15 | 24600.00 | 1132.6 |
| 293.15 | 29670.00 | 1134.6 |
| 293.15 | 34600.00 | 1136.6 |
| 293.15 | 39380.00 | 1138.5 |
| 293.15 | 44310.00 | 1140.4 |
| 293.15 | 49240.00 | 1142.3 |
| 293.15 | 54080.00 | 1144.1 |
| 293.15 | 58950.00 | 1145.9 |
| 293.15 | 63910.00 | 1147.7 |
| 293.15 | 68760.00 | 1149.4 |
| 303.15 | 100.00 | 1114.0 |
| 303.15 | 100.00 | 1114.0 |
| 303.15 | 630.00 | 1114.2 |
| 303.15 | 1200.00 | 1114.5 |
| 303.15 | 1610.00 | 1114.7 |
| 303.15 | 2120.00 | 1114.9 |
| 303.15 | 3090.00 | 1115.4 |
| 303.15 | 5080.00 | 1116.3 |
| 303.15 | 7050.00 | 1117.2 |
| 303.15 | 10000.00 | 1118.5 |
| 303.15 | 14920.00 | 1120.8 |
| 303.15 | 19740.00 | 1122.9 |
| 303.15 | 24580.00 | 1125.0 |
| 303.15 | 29520.00 | 1127.1 |
| 303.15 | 34410.00 | 1129.1 |
| 303.15 | 39420.00 | 1131.2 |
| 303.15 | 44270.00 | 1133.1 |
| 303.15 | 49210.00 | 1135.1 |
| 303.15 | 54140.00 | 1136.9 |
| 303.15 | 59090.00 | 1138.8 |
| 303.15 | 63880.00 | 1140.6 |
| 303.15 | 68800.00 | 1142.4 |
| 313.15 | 100.00 | 1106.0 |
| 313.15 | 100.00 | 1106.0 |
| 313.15 | 570.00 | 1106.3 |
| 313.15 | 1110.00 | 1106.5 |
| 313.15 | 1570.00 | 1106.7 |
| 313.15 | 2100.00 | 1107.0 |
| 313.15 | 3080.00 | 1107.5 |
| 313.15 | 5070.00 | 1108.4 |
| 313.15 | 7000.00 | 1109.4 |
| 313.15 | 9960.00 | 1110.7 |
| 313.15 | 14830.00 | 1113.0 |
| 313.15 | 19730.00 | 1115.2 |
| 313.15 | 24720.00 | 1117.5 |
| 313.15 | 29640.00 | 1119.6 |
| 313.15 | 34400.00 | 1121.8 |
| 313.15 | 39380.00 | 1123.8 |
| 313.15 | 44210.00 | 1125.9 |
| 313.15 | 49240.00 | 1127.8 |
| 313.15 | 54040.00 | 1129.8 |
| 313.15 | 59030.00 | 1131.7 |
| 313.15 | 63920.00 | 1133.6 |
| 313.15 | 68770.00 | 1135.4 |
| 323.15 | 100.00 | 1098.0 |
| 323.15 | 100.00 | 1098.0 |
| 323.15 | 590.00 | 1098.3 |
| 323.15 | 1180.00 | 1098.5 |
| 323.15 | 1580.00 | 1098.8 |
| 323.15 | 2100.00 | 1099.0 |
| 323.15 | 3000.00 | 1099.5 |
| 323.15 | 5060.00 | 1100.5 |
| 323.15 | 7010.00 | 1101.5 |
| 323.15 | 9930.00 | 1102.9 |
| 323.15 | 14900.00 | 1105.3 |
| 323.15 | 19770.00 | 1107.6 |
| 323.15 | 24760.00 | 1110.0 |
| 323.15 | 29530.00 | 1112.1 |
| 323.15 | 34470.00 | 1114.4 |
| 323.15 | 39440.00 | 1116.5 |
| 323.15 | 44180.00 | 1118.6 |
| 323.15 | 49200.00 | 1120.6 |
| 323.15 | 54100.00 | 1122.7 |
| 323.15 | 58970.00 | 1124.6 |
| 323.15 | 63800.00 | 1126.5 |
| 323.15 | 68790.00 | 1128.4 |
| 333.15 | 100.00 | 1090.1 |
| 333.15 | 100.00 | 1090.1 |
| 333.15 | 660.00 | 1090.4 |
| 333.15 | 1170.00 | 1090.6 |
| 333.15 | 1590.00 | 1090.8 |
| 333.15 | 2110.00 | 1091.1 |
| 333.15 | 3020.00 | 1091.6 |
| 333.15 | 5110.00 | 1092.7 |
| 333.15 | 6990.00 | 1093.7 |
| 333.15 | 9900.00 | 1095.1 |
| 333.15 | 14860.00 | 1097.7 |
| 333.15 | 19730.00 | 1100.0 |
| 333.15 | 23990.00 | 1102.6 |
| 333.15 | 29600.00 | 1104.7 |
| 333.15 | 34450.00 | 1107.1 |
| 333.15 | 39370.00 | 1109.2 |
| 333.15 | 44310.00 | 1111.5 |
| 333.15 | 49120.00 | 1113.5 |
| 333.15 | 54060.00 | 1115.6 |
| 333.15 | 59100.00 | 1117.7 |
| 333.15 | 63900.00 | 1119.7 |
| 333.15 | 68790.00 | 1121.6 |
| 343.15 | 100.00 | 1082.1 |
| 343.15 | 100.00 | 1082.1 |
| 343.15 | 720.00 | 1082.5 |
| 343.15 | 1090.00 | 1082.7 |
| 343.15 | 1600.00 | 1082.9 |
| 343.15 | 2060.00 | 1083.2 |
| 343.15 | 3100.00 | 1083.7 |
| 343.15 | 5040.00 | 1084.8 |
| 343.15 | 6870.00 | 1085.8 |
| 343.15 | 9930.00 | 1087.4 |
| 343.15 | 14830.00 | 1090.0 |
| 343.15 | 19790.00 | 1092.5 |
| 343.15 | 24630.00 | 1095.0 |
| 343.15 | 29580.00 | 1097.4 |
| 343.15 | 34440.00 | 1099.7 |
| 343.15 | 39430.00 | 1102.1 |
| 343.15 | 44410.00 | 1104.4 |
| 343.15 | 49170.00 | 1106.5 |
| 343.15 | 54160.00 | 1108.6 |
| 343.15 | 58970.00 | 1110.7 |
| 343.15 | 63920.00 | 1112.8 |
| 343.15 | 68720.00 | 1114.7 |
| 353.15 | 100.00 | 1074.1 |
| 353.15 | 100.00 | 1074.1 |
| 353.15 | 560.00 | 1074.4 |
| 353.15 | 1190.00 | 1074.7 |
| 353.15 | 1660.00 | 1075.0 |
| 353.15 | 2160.00 | 1075.3 |
| 353.15 | 3100.00 | 1075.8 |
| 353.15 | 5040.00 | 1076.9 |
| 353.15 | 6910.00 | 1078.0 |
| 353.15 | 10040.00 | 1079.7 |
| 353.15 | 14770.00 | 1082.3 |
| 353.15 | 19790.00 | 1085.0 |
| 353.15 | 24570.00 | 1087.5 |
| 353.15 | 29460.00 | 1090.0 |
| 353.15 | 34560.00 | 1092.5 |
| 353.15 | 39340.00 | 1094.8 |
| 353.15 | 44310.00 | 1097.2 |
| 353.15 | 49190.00 | 1099.5 |
| 353.15 | 54020.00 | 1101.6 |
| 353.15 | 59160.00 | 1103.9 |
| 353.15 | 63870.00 | 1106.0 |
| 353.15 | 68800.00 | 1108.0 |
| 363.15 | 100.00 | 1066.1 |
| 363.15 | 100.00 | 1066.1 |
| 363.15 | 650.00 | 1066.5 |
| 363.15 | 1150.00 | 1066.7 |
| 363.15 | 1550.00 | 1067.0 |
| 363.15 | 2070.00 | 1067.2 |
| 363.15 | 3090.00 | 1067.9 |
| 363.15 | 5060.00 | 1069.0 |
| 363.15 | 7010.00 | 1070.2 |
| 363.15 | 9860.00 | 1071.8 |
| 363.15 | 14820.00 | 1074.7 |
| 363.15 | 19750.00 | 1077.4 |
| 363.15 | 24740.00 | 1080.1 |
| 363.15 | 29560.00 | 1082.6 |
| 363.15 | 34540.00 | 1085.2 |
| 363.15 | 39360.00 | 1087.6 |
| 363.15 | 44280.00 | 1090.1 |
| 363.15 | 49130.00 | 1092.3 |
| 363.15 | 54040.00 | 1094.7 |
| 363.15 | 59030.00 | 1097.0 |
| 363.15 | 63900.00 | 1099.1 |
| 363.15 | 68810.00 | 1101.6 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [2.28e-10; 2622.24] | kPa | [268.15; 722.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 2.51044e+02 | |||
| Coefficient B | -2.43857e+04 | |||
| Coefficient C | -3.27566e+01 | |||
| Coefficient D | 1.19079e-05 | |||
| Temperature range, min. | 268.15 | |||
| Temperature range, max. | 722.00 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 400 600 | ||||
| Pvap | 2.28e-10 | kPa | 268.15 | Calculated Property |
| Pvap | 2.05e-06 | kPa | 318.58 | Calculated Property |
| Pvap | 8.79e-04 | kPa | 369.01 | Calculated Property |
| Pvap | 0.06 | kPa | 419.43 | Calculated Property |
| Pvap | 1.27 | kPa | 469.86 | Calculated Property |
| Pvap | 12.50 | kPa | 520.29 | Calculated Property |
| Pvap | 73.12 | kPa | 570.72 | Calculated Property |
| Pvap | 299.82 | kPa | 621.14 | Calculated Property |
| Pvap | 963.43 | kPa | 671.57 | Calculated Property |
| Pvap | 2622.24 | kPa | 722.00 | 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,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)
![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 Tetraethylene glycol.
Mixtures
- Tetraethylene glycol + lithium chloride + Water
- lithium bromide + Tetraethylene glycol + Water
- Tetraethylene glycol + Tromethamine + Water
- Tetraethylene glycol + Water
- Ethanol + Tetraethylene glycol
- Magnesium chloride + Tetraethylene glycol + Water
- Benzene + Tetraethylene glycol
- Toluene + Tetraethylene glycol
- Tetraethylene glycol + Ethylbenzene
- Tetraethylene glycol + Heptane
- Tetraethylene glycol + Octane
- Tetraethylene glycol + Nonane
- Tetraethylene glycol + Decane
- Tetraethylene glycol + Dimethyl Sulfoxide
- Benzyl alcohol + Tetraethylene glycol
- Tetraethylene glycol + Phenylethyl Alcohol
- Carbon dioxide + Tetraethylene glycol
- Tetraethylene glycol + Heptane + o-Xylene
- Tetraethylene glycol + Thiophene + Octane
Sources
- 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
- Mutual diffusion coefficients of aqueous solutions of some glycols
- The effect of the end group, molecular weight and size on the solubility of compounds in supercritical carbon dioxide
- 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
- Vapour pressures and densities of the mixed-solvent desiccants (glycols + water + salts)
- Densities and vapor pressures of mixed-solvent desiccant systems containing {glycol (diethylene, or triethylene, or tetraethylene glycol) + salt (magnesium chloride) + water}
- 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}
- Volumetric and acoustic studies on (tetraethylene glycol + water) mixtures in a wide temperature range
- 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)
- 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
- 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
- Measurement and Modeling of Isobaric Vapor-Liquid Equilibrium of Water + Glycols
- Infinite Dilution Activity Coefficients of Hydrocarbons in Triethylene Glycol and Tetraethylene Glycol
- Excess Molar Enthalpies of Binary Mixtures Containing Glycols or Polyglycols + Dimethyl Sulfoxide at 308.15 K
- Analysis and Evaluation of the Liquid-Liquid Equilibrium Data of the Extraction of Aromatics from Hydrocarbons by Tetraethylene Glycol
- 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 of Ternary Systems Sulfide + Octane + Solvents at Different Temperatures
- Solubility Comparison of Bis(2-hydroxyethyl) Ether and Tetraethylene Glycol before and after End-Group Modification by Ethyl Oxalyl Chloride in Supercritical Carbon Dioxide
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more. Take the time to validate and double check the source of the data.