Chemical Properties of Hexaethylene glycol (CAS 2615-15-8)

Hexaethylene glycol

InChI
InChI=1S/C12H26O7/c13-1-3-15-5-7-17-9-11-19-12-10-18-8-6-16-4-2-14/h13-14H,1-12H2
InChI Key
IIRDTKBZINWQAW-UHFFFAOYSA-N
Formula
C12H26O7
SMILES
OCCOCCOCCOCCOCCOCCO
Molecular Weight1
282.33
CAS
2615-15-8
Other Names
  • 2-[2-[2-[2-[2-(2-Hydroxyethoxy)ethoxy]ethoxy]ethoxy]ethoxy]ethanol
  • 3,6,9,12,15-pentaoxaheptadecane-1,17-diol
  • Ethanol, 2,2'-(oxybis(ethyleneoxyethyleneoxy))di-
  • Ethanol, 2,2'-(oxybis(oxy-2,1-ethanediyloxy-2,1-ethanediyloxy))bis-
  • Hexagol
  • Hexaoxyethylene glycol
  • NSC 201209
  • PEG-6
  • Polyethylene glycol 300
  • Polyoxyethylene (6)
  • ethanol, 2,2'-[oxybis(ethyleneoxyethyleneoxy)]di-
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Physical Properties

Property Value Unit Source
ω 0.5542 ChemSep v8.3 pure component data Compiled value
ΔfG° -161.43 kJ/mol ChemSep v8.3 pure component data Compiled value
ΔfH°gas -469.11 kJ/mol ChemSep v8.3 pure component data Compiled value
ΔfusH° 40.95 kJ/mol Joback Calculated Property
ΔvapH° 105.82 kJ/mol Relay (1.0) Calculated Property
IE 9.77 eV Relay (1.0) Calculated Property
log10WS 0.29 Relay (1.0) Calculated Property
logPoct/wat -0.946 Crippen Calculated Property
McVol 221.030 ml/mol McGowan Calculated Property
Pc 1746.24 kPa ChemSep v8.3 pure component data Compiled value
Inp [2078.00; 2081.80]   Show Hide
Inp 2078.00 NIST
Inp 2081.80 NIST
Inp 2081.80 NIST
Inp 2078.00 NIST
Tboil 618.25 K ChemSep v8.3 pure component data Compiled value
Tc [773.64; 868.00] K Show Hide
Tc 868.00 K Critical temperatures and pressures of ethylene glycols
Tc 773.64 K ChemSep v8.3 pure component data Compiled value
Tfus [274.45; 279.15] K Show Hide
Tfus 279.15 K Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus 274.45 K ChemSep v8.3 pure component data Compiled value
Tfus 274.45 ± 0.70 K NIST
Ttriple 280.80 K Heat Capacity and Phase Behavior of Selected Oligo(ethylene glycol)s
UQi 8.85 ChemSep v8.3 pure component data Compiled value
URi 10.37 ChemSep v8.3 pure component data Compiled value
Vc 0.828 m3/kmol ChemSep v8.3 pure component data Compiled value
Zc 0.2248110 ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property Value Unit Temperature (K) Source
Cp,liquid 620.00 J/mol×K 298.00 NIST

Datasets

Mass density, kg/m3

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mass density, kg/m3 - Liquid
283.13 100.00 1134.5
283.13 1000.00 1134.8
283.13 2000.00 1135.1
283.13 5000.00 1136.4
283.13 7000.00 1137.3
283.13 10000.00 1138.5
283.13 12000.00 1139.3
283.13 16000.00 1141.1
283.13 20000.00 1142.8
283.13 25000.00 1144.6
283.13 30000.00 1146.5
283.13 35000.00 1148.5
283.13 40000.00 1150.6
283.13 45000.00 1152.6
283.13 50000.00 1154.4
283.13 55000.00 1156.4
283.13 60000.00 1158.4
283.13 65000.00 1160.0
283.13 70000.00 1161.8
283.13 75000.00 1163.6
283.13 80000.00 1165.3
283.13 85000.00 1167.1
283.13 90000.00 1168.7
283.13 95000.00 1170.5
293.16 100.00 1125.6
293.16 1000.00 1126.0
293.16 2000.00 1126.5
293.16 5000.00 1127.9
293.16 7000.00 1128.9
293.16 10000.00 1130.3
293.16 12000.00 1131.1
293.16 16000.00 1132.9
293.16 20000.00 1134.6
293.16 25000.00 1136.8
293.16 30000.00 1138.3
293.16 35000.00 1140.8
293.16 40000.00 1143.1
293.16 45000.00 1144.9
293.16 50000.00 1146.9
293.16 55000.00 1148.9
293.16 60000.00 1150.8
293.16 65000.00 1152.8
293.16 70000.00 1154.6
293.16 75000.00 1156.4
293.16 80000.00 1158.3
293.16 85000.00 1160.0
293.16 90000.00 1161.7
293.16 95000.00 1163.5
303.15 100.00 1117.5
303.15 1000.00 1118.0
303.15 2000.00 1118.5
303.15 5000.00 1120.0
303.15 7000.00 1120.8
303.15 10000.00 1122.3
303.15 12000.00 1123.2
303.15 16000.00 1124.9
303.15 20000.00 1126.8
303.15 25000.00 1129.1
303.15 30000.00 1131.2
303.15 35000.00 1133.4
303.15 40000.00 1135.4
303.15 45000.00 1137.5
303.15 50000.00 1139.4
303.15 55000.00 1141.6
303.15 60000.00 1143.4
303.15 65000.00 1145.2
303.15 70000.00 1147.2
303.15 75000.00 1149.1
303.15 80000.00 1150.8
303.15 85000.00 1152.9
303.15 90000.00 1154.8
303.15 95000.00 1156.4
313.16 100.00 1109.2
313.16 1000.00 1109.7
313.16 2000.00 1110.2
313.16 5000.00 1111.9
313.16 7000.00 1112.8
313.16 10000.00 1114.3
313.16 12000.00 1115.2
313.16 16000.00 1117.1
313.16 20000.00 1119.0
313.16 25000.00 1121.3
313.16 30000.00 1123.4
313.16 35000.00 1125.7
313.16 40000.00 1127.8
313.16 45000.00 1129.9
313.16 50000.00 1132.0
313.16 55000.00 1134.2
313.16 60000.00 1135.7
313.16 65000.00 1138.1
313.16 70000.00 1140.0
313.16 75000.00 1142.1
313.16 80000.00 1144.0
313.16 85000.00 1145.9
313.16 90000.00 1147.8
313.16 95000.00 1149.7
323.14 100.00 1100.9
323.14 1000.00 1101.3
323.14 2000.00 1101.8
323.14 5000.00 1103.5
323.14 7000.00 1104.5
323.14 10000.00 1106.0
323.14 12000.00 1106.9
323.14 16000.00 1109.0
323.14 20000.00 1110.5
323.14 25000.00 1113.2
323.14 30000.00 1115.6
323.14 35000.00 1118.0
323.14 40000.00 1120.2
323.14 45000.00 1122.4
323.14 50000.00 1124.5
323.14 55000.00 1126.4
323.14 60000.00 1128.5
323.14 65000.00 1130.6
323.14 70000.00 1132.6
323.14 75000.00 1134.6
323.14 80000.00 1136.8
323.14 85000.00 1138.6
323.14 90000.00 1140.7
323.14 95000.00 1142.4
333.15 100.00 1092.7
333.15 1000.00 1093.3
333.15 2000.00 1093.8
333.15 5000.00 1095.4
333.15 7000.00 1096.5
333.15 10000.00 1098.2
333.15 12000.00 1099.1
333.15 16000.00 1101.3
333.15 20000.00 1103.4
333.15 25000.00 1105.8
333.15 30000.00 1108.2
333.15 35000.00 1110.5
333.15 40000.00 1112.8
333.15 45000.00 1115.1
333.15 50000.00 1117.3
333.15 55000.00 1119.4
333.15 60000.00 1121.7
333.15 65000.00 1123.7
333.15 70000.00 1125.5
333.15 75000.00 1127.8
333.15 80000.00 1130.0
333.15 85000.00 1131.9
333.15 90000.00 1133.8
333.15 95000.00 1135.7
343.16 100.00 1084.7
343.16 1000.00 1085.3
343.16 2000.00 1085.9
343.16 5000.00 1087.6
343.16 7000.00 1088.7
343.16 10000.00 1090.4
343.16 12000.00 1091.2
343.16 16000.00 1093.5
343.16 20000.00 1095.7
343.16 25000.00 1097.9
343.16 30000.00 1100.5
343.16 35000.00 1102.8
343.16 40000.00 1105.4
343.16 45000.00 1107.6
343.16 50000.00 1109.9
343.16 55000.00 1112.1
343.16 60000.00 1114.5
343.16 65000.00 1116.6
343.16 70000.00 1118.8
343.16 75000.00 1120.9
343.16 80000.00 1123.1
343.16 85000.00 1125.2
343.16 90000.00 1127.2
343.16 95000.00 1129.2
353.14 100.00 1076.7
353.14 1000.00 1077.2
353.14 2000.00 1077.9
353.14 5000.00 1079.7
353.14 7000.00 1080.7
353.14 10000.00 1082.4
353.14 12000.00 1083.6
353.14 16000.00 1085.7
353.14 20000.00 1087.8
353.14 25000.00 1090.4
353.14 30000.00 1093.0
353.14 35000.00 1095.6
353.14 40000.00 1098.2
353.14 45000.00 1100.3
353.14 50000.00 1102.7
353.14 55000.00 1105.0
353.14 60000.00 1107.4
353.14 65000.00 1109.6
353.14 70000.00 1111.8
353.14 75000.00 1114.2
353.14 80000.00 1116.1
353.14 85000.00 1118.3
353.14 90000.00 1120.3
353.14 95000.00 1122.4
363.13 100.00 1068.4
363.13 1000.00 1068.6
363.13 2000.00 1069.0
363.13 5000.00 1071.6
363.13 7000.00 1072.7
363.13 10000.00 1074.6
363.13 12000.00 1075.6
363.13 16000.00 1078.0
363.13 20000.00 1080.2
363.13 25000.00 1083.0
363.13 30000.00 1085.4
363.13 35000.00 1088.1
363.13 40000.00 1090.6
363.13 45000.00 1092.7
363.13 50000.00 1095.2
363.13 55000.00 1097.6
363.13 60000.00 1100.1
363.13 65000.00 1102.5
363.13 70000.00 1104.8
363.13 75000.00 1107.0
363.13 80000.00 1109.2
363.13 85000.00 1111.2
363.13 90000.00 1113.5
363.13 95000.00 1115.6
Reference

Correlations

Property Value Unit Temperature (K) Source
Cp,gas [304.79; 874.60] J/mol×K [255.00; 1500.00] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is Cp,gas in J/mol×K, T in K
Coefficient A1.65506e+02
Coefficient B-5.00000e+02
Coefficient C6.89731e+00
Coefficient D0.00000e+00
Coefficient E0.00000e+00
Temperature range, min.255.00
Temperature range, max.1500.00
Cp,gas 304.79 J/mol×K 255.00 Calculated Property
Cp,gas 443.09 J/mol×K 393.33 Calculated Property
Cp,gas 551.91 J/mol×K 531.67 Calculated Property
Cp,gas 634.71 J/mol×K 670.00 Calculated Property
Cp,gas 698.63 J/mol×K 808.33 Calculated Property
Cp,gas 749.06 J/mol×K 946.67 Calculated Property
Cp,gas 789.71 J/mol×K 1085.00 Calculated Property
Cp,gas 823.10 J/mol×K 1223.33 Calculated Property
Cp,gas 850.98 J/mol×K 1361.67 Calculated Property
Cp,gas 874.60 J/mol×K 1500.00 Calculated Property
Property Value Unit Temperature (K) Source
η [0.9040725; 0.0000294] Pa×s [276.02; 574.57] Joback Predicted correlation Show Hide
EquationY = exp(A + B/T + C·ln(T) + D·T^E)
Y is η in Pa×s, T in K
Coefficient A-1.99909e+01
Coefficient B5.48999e+03
Coefficient C0.00000e+00
Coefficient D0.00000e+00
Coefficient E0.00000e+00
CommentLiquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc.
Temperature range, min.276.02
Temperature range, max.574.57
η 0.9040725 Pa×s 276.02 Calculated Property
η 0.1070072 Pa×s 309.19 Calculated Property
η 0.0191525 Pa×s 342.36 Calculated Property
η 0.0046456 Pa×s 375.54 Calculated Property
η 0.0014182 Pa×s 408.71 Calculated Property
η 0.0005173 Pa×s 441.88 Calculated Property
η 0.0002173 Pa×s 475.06 Calculated Property
η 0.0001022 Pa×s 508.23 Calculated Property
η 0.0000527 Pa×s 541.40 Calculated Property
η 0.0000294 Pa×s 574.57 Calculated Property

Similar Compounds

3,6,9,12,15,18,21,24,27-nonaoxanonacosane-1,29-diol. Tetraethylene glycol. 3,6,9,12,15,18,21,24,27,30-decaoxadotriacontane-1,32-diol. Octaethylene glycol. Triethylene glycol. 3,6,9,12,15,18,21,24-octaoxahexacosane-1,26-diol. 2-[2-[2-[2-[2-[2-[2-[2-[2-[2-[2-(2-Hydroxyethoxy)ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethanol. Heptaethylene glycol. 3,6,9,12-TETRAOXATETRADECANE-1,14-DIOL. 2-[2-[2-[2-[2-[2-[2-[2-[2-[2-(2-Methoxyethoxy)ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethanol. 2-[2-[2-[2-[2-[2-(2-Methoxyethoxy)ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethanol. 2,5,8,11,14-Pentaoxahexadecan-16-ol. Ethanol, 2-[2-(2-methoxyethoxy)ethoxy]-. 2-[2-[2-[2-[2-[2-[2-[2-(2-Methoxyethoxy)ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethanol. Hexaethylene glycol monomethyl ether.

Find more compounds similar to Hexaethylene glycol.

Sources

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