Physical Properties
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
Equation Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K
Coefficient A 1.65506e+02
Coefficient B -5.00000e+02
Coefficient C 6.89731e+00
Coefficient D 0.00000e+00
Coefficient E 0.00000e+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
Equation Y = 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 B 5.48999e+03
Coefficient C 0.00000e+00
Coefficient D 0.00000e+00
Coefficient E 0.00000e+00
Comment Liquid 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
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