Contents
Physical Properties
Temperature Dependent Properties
Datasets
Correlations
Similar Compounds
Mixtures
Sources
Physical Properties
Property
Value
Unit
Source
Δf G°
-218.74
kJ/mol
Joback Calculated Property
Δf H°gas
-813.79
kJ/mol
Joback Calculated Property
Δfus H°
50.10
kJ/mol
Joback Calculated Property
Δvap H°
89.49
kJ/mol
Joback Calculated Property
log 10 WS
[-7.06; -6.96]
log 10 WS
-7.06
Aq. Sol...
log 10 WS
-6.96
Estimat...
log Poct/wat
6.433
Crippen Calculated Property
McVol
340.140
ml/mol
McGowan Calculated Property
Pc
1070.00
kPa
Critica...
Inp
[402.20; 2552.00]
Inp
2492.60
NIST
Inp
2509.00
NIST
Inp
2507.00
NIST
Inp
2499.40
NIST
Inp
2499.00
NIST
Inp
2499.00
NIST
Inp
2505.00
NIST
Inp
2546.00
NIST
Inp
2488.00
NIST
Inp
2498.00
NIST
Inp
2552.00
NIST
Inp
2539.00
NIST
Inp
2544.00
NIST
Inp
2551.00
NIST
Inp
2509.00
NIST
Inp
2550.00
NIST
Inp
2519.00
NIST
Inp
2504.00
NIST
Inp
2505.00
NIST
Inp
2506.00
NIST
Inp
2480.00
NIST
Inp
2505.00
NIST
Inp
2506.00
NIST
Inp
2509.00
NIST
Inp
2506.00
NIST
Inp
2507.00
NIST
Inp
Outlier 418.60
NIST
Inp
Outlier 418.70
NIST
Inp
Outlier 402.20
NIST
Inp
Outlier 406.14
NIST
Inp
Outlier 406.15
NIST
Inp
2488.00
NIST
Inp
2505.00
NIST
Inp
2492.60
NIST
Inp
Outlier 418.60
NIST
Inp
2499.40
NIST
Inp
2507.00
NIST
Inp
Outlier 406.14
NIST
Inp
2539.00
NIST
Inp
2519.00
NIST
I
[3106.00; 3106.00]
I
3106.00
NIST
I
3106.00
NIST
I
3106.00
NIST
I
3106.00
NIST
I
3106.00
NIST
S°liquid
[755.20; 807.70]
J/mol×K
S°liquid
807.70
J/mol×K
NIST
S°liquid
755.20
J/mol×K
NIST
Tboil
657.20
K
NIST
Tc
1142.43
K
Joback Calculated Property
Tfus
219.82
K
Aq. Sol...
Vc
1.308
m3 /kmol
Joback Calculated Property
Temperature Dependent Properties
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[1120.29; 1202.19]
J/mol×K
[931.88; 1142.43]
Cp,gas
1120.29
J/mol×K
931.88
Joback Calculated Property
Cp,gas
1137.32
J/mol×K
966.97
Joback Calculated Property
Cp,gas
1152.94
J/mol×K
1002.06
Joback Calculated Property
Cp,gas
1167.20
J/mol×K
1037.16
Joback Calculated Property
Cp,gas
1180.14
J/mol×K
1072.25
Joback Calculated Property
Cp,gas
1191.79
J/mol×K
1107.34
Joback Calculated Property
Cp,gas
1202.19
J/mol×K
1142.43
Joback Calculated Property
Cp,liquid
[669.40; 704.70]
J/mol×K
[298.15; 300.00]
Cp,liquid
704.70
J/mol×K
298.15
NIST
Cp,liquid
669.40
J/mol×K
300.00
NIST
η
[0.0061990; 0.1107000]
Pa×s
[288.53; 353.68]
η
0.1107000
Pa×s
288.53
Measure...
η
0.0787300
Pa×s
293.38
Measure...
η
0.0579400
Pa×s
298.29
Measure...
η
0.0432700
Pa×s
303.33
Measure...
η
0.0331700
Pa×s
308.23
Measure...
η
0.0261300
Pa×s
313.18
Measure...
η
0.0210800
Pa×s
317.99
Measure...
η
0.0169600
Pa×s
323.02
Measure...
η
0.0139100
Pa×s
328.12
Measure...
η
0.0116200
Pa×s
333.19
Measure...
η
0.0099030
Pa×s
337.71
Measure...
η
0.0082680
Pa×s
343.53
Measure...
η
0.0071580
Pa×s
348.48
Measure...
η
0.0061990
Pa×s
353.68
Measure...
Δvap H
[102.50; 116.90]
kJ/mol
[298.00; 516.50]
Δvap H
116.90
kJ/mol
298.00
A Compa...
Δvap H
110.70
kJ/mol
412.50
NIST
Δvap H
102.50
kJ/mol
516.50
NIST
Pvap
[8.00e-03; 0.19]
kPa
[423.15; 473.15]
Pvap
8.00e-03
kPa
423.15
Vapor P...
Pvap
0.02
kPa
433.15
Vapor P...
Pvap
0.03
kPa
443.15
Vapor P...
Pvap
0.04
kPa
448.15
Vapor P...
Pvap
0.07
kPa
453.15
Vapor P...
Pvap
0.12
kPa
463.15
Vapor P...
Pvap
0.19
kPa
473.15
Vapor P...
ρl
[931.85; 998.82]
kg/m3
[273.15; 363.15]
ρl
998.82
kg/m3
273.15
Tempera...
ρl
995.01
kg/m3
278.15
Tempera...
ρl
991.26
kg/m3
283.15
Tempera...
ρl
983.87
kg/m3
293.15
Tempera...
ρl
980.15
kg/m3
298.15
Tempera...
ρl
976.42
kg/m3
303.15
Tempera...
ρl
968.98
kg/m3
313.15
Tempera...
ρl
961.53
kg/m3
323.15
Tempera...
ρl
954.11
kg/m3
333.15
Tempera...
ρl
946.68
kg/m3
343.15
Tempera...
ρl
939.27
kg/m3
353.15
Tempera...
ρl
931.85
kg/m3
363.15
Tempera...
D* i
[0.00; 0.00]
m2 /s
[303.18; 362.75]
D* i
0.00
m2 /s
303.18
Viscous...
D* i
0.00
m2 /s
312.89
Viscous...
D* i
0.00
m2 /s
322.70
Viscous...
D* i
0.00
m2 /s
322.84
Viscous...
D* i
0.00
m2 /s
322.88
Viscous...
D* i
0.00
m2 /s
323.03
Viscous...
D* i
0.00
m2 /s
323.05
Viscous...
D* i
0.00
m2 /s
333.16
Viscous...
D* i
0.00
m2 /s
333.20
Viscous...
D* i
0.00
m2 /s
343.65
Viscous...
D* i
0.00
m2 /s
343.70
Viscous...
D* i
0.00
m2 /s
352.86
Viscous...
D* i
0.00
m2 /s
352.88
Viscous...
D* i
0.00
m2 /s
362.72
Viscous...
D* i
0.00
m2 /s
362.75
Viscous...
Datasets
Molar heat capacity at constant pressure, J/K/mol (1)
Mass density, kg/m3 (1)
Molar heat capacity at constant pressure, J/K/mol
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Molar heat capacity at constant pressure, J/K/mol - Liquid
293.15
100.00
703.00
293.15
10000.00
701.50
293.15
20000.00
699.90
293.15
30000.00
699.60
313.15
100.00
726.90
313.15
10000.00
724.90
313.15
20000.00
723.00
313.15
30000.00
722.00
333.15
100.00
751.30
333.15
10000.00
750.00
333.15
20000.00
747.50
333.15
30000.00
746.00
353.15
100.00
774.50
353.15
10000.00
770.50
353.15
20000.00
767.90
353.15
30000.00
763.40
Reference
Mass density, kg/m3
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Mass density, kg/m3 - Liquid
373.29
3800.00
921.0
373.29
7600.00
924.0
373.29
12200.00
928.0
373.29
15900.00
931.0
373.29
18100.00
933.0
373.29
22300.00
936.0
373.29
28300.00
940.0
373.29
34800.00
945.0
373.29
42200.00
950.0
373.29
48900.00
954.0
373.29
56100.00
959.0
373.29
69500.00
967.0
373.29
83700.00
974.0
373.29
104200.00
984.0
373.29
125400.00
994.0
373.29
138900.00
1001.0
373.29
152900.00
1007.0
373.29
174400.00
1015.0
373.29
208300.00
1029.0
373.29
240000.00
1041.0
373.29
262100.00
1046.0
423.53
4200.00
878.0
423.53
7900.00
885.0
423.53
11100.00
890.0
423.53
14500.00
895.0
423.53
18000.00
898.0
423.53
21200.00
901.0
423.53
27800.00
908.0
423.53
35200.00
914.0
423.53
42100.00
918.0
423.53
49200.00
924.0
423.53
55700.00
930.0
423.53
70700.00
939.0
423.53
83700.00
948.0
423.53
104200.00
960.0
423.53
125400.00
970.0
423.53
139900.00
977.0
423.53
153700.00
983.0
423.53
173400.00
992.0
423.53
207100.00
1006.0
423.53
239400.00
1018.0
423.53
263800.00
1028.0
476.20
5500.00
847.0
476.20
9500.00
853.0
476.20
9400.00
853.0
476.20
15700.00
861.0
476.20
15200.00
861.0
476.20
15200.00
861.0
476.20
27500.00
874.0
476.20
27300.00
874.0
476.20
26800.00
874.0
476.20
46900.00
894.0
476.20
46700.00
894.0
476.20
59800.00
905.0
476.20
71500.00
913.0
476.20
70700.00
914.0
476.20
96400.00
931.0
476.20
95700.00
931.0
476.20
114800.00
942.0
476.20
114200.00
942.0
476.20
140400.00
958.0
476.20
139800.00
959.0
476.20
176200.00
975.0
476.20
206900.00
990.0
476.20
240200.00
1002.0
476.20
269000.00
1013.0
491.86
3900.00
830.0
491.86
4100.00
830.0
491.86
3900.00
831.0
491.86
10500.00
839.0
491.86
9900.00
840.0
491.86
23300.00
856.0
491.86
23300.00
856.0
491.86
22800.00
856.0
491.86
37500.00
870.0
491.86
37200.00
870.0
491.86
51100.00
885.0
491.86
50700.00
886.0
491.86
71500.00
902.0
491.86
71900.00
902.0
491.86
95000.00
918.0
491.86
94800.00
918.0
491.86
121700.00
934.0
491.86
121800.00
934.0
491.86
145400.00
948.0
491.86
145600.00
948.0
491.86
177200.00
964.0
491.86
177400.00
964.0
491.86
204300.00
977.0
491.86
206000.00
978.0
491.86
230800.00
988.0
491.86
229400.00
989.0
491.86
253700.00
998.0
491.86
258100.00
1000.0
523.60
5700.00
811.0
523.60
9200.00
817.0
523.60
9200.00
817.0
523.60
16100.00
827.0
523.60
16100.00
827.0
523.60
21600.00
835.0
523.60
21600.00
835.0
523.60
27500.00
842.0
523.60
27300.00
842.0
523.60
35700.00
851.0
523.60
35500.00
851.0
523.60
44400.00
860.0
523.60
44600.00
860.0
523.60
44300.00
860.0
523.60
44200.00
860.0
523.60
56300.00
871.0
523.60
55800.00
871.0
523.60
68900.00
882.0
523.60
68500.00
882.0
523.60
82500.00
892.0
523.60
82200.00
893.0
523.60
97300.00
903.0
523.60
97000.00
903.0
523.60
117000.00
916.0
523.60
117700.00
916.0
523.60
117400.00
916.0
523.60
155700.00
939.0
523.60
156100.00
939.0
523.60
181500.00
952.0
523.60
181200.00
952.0
523.60
209500.00
964.0
523.60
209900.00
964.0
523.60
233900.00
974.0
523.60
234000.00
974.0
523.60
253600.00
983.0
523.60
253400.00
983.0
523.60
263500.00
987.0
Reference
Correlations
Similar Compounds
Find more compounds similar to Bis(2-ethylhexyl) phthalate .
Mixtures
Sources
KDB Vapor Pressure Data
Crippen Method
An experimental setup for isobaric heat capacities for viscous fluids at high pressure: Squalane, bis(2-ethylhexyl) sebacate and bis(2-ethylhexyl) phthalate
Experimental density measurements of bis(2-ethylhexyl) phthalate at elevated temperatures and pressures
Viscous Calibration Liquids for Self-diffusion Measurements
A Comparison of Results by Correlation Gas Chromatography with Another Gas Chromatographic Retention Time Technique. The Effects of Retention Time Coincidence on Vaporization Enthalpy and Vapor Pressure
Solubilities at High Dilution of Toluene, Ethylbenzene, 1,2,4-Trimethylbenzene, and Hexane in Di-2-ethylhexyl, Diisoheptyl, and Diisononyl Phthalates
Critical Temperatures and Pressures of 12 Phthalates Using the Pulse-Heating Method
Measurements of the Viscosity of Bis(2-ethylhexyl) Sebacate, Squalane, and Bis(2-ethylhexyl) Phthalate between (283 and 363) K at 0.1 MPa
Vapor Pressure and Enthalpy of Vaporization of Fentanyl
Temperature and Pressure Dependence of the Viscosities of 2-Ethylhexyl Benzoate, Bis(2-ethylhexyl) Phthalate, 2,6,10,15,19,23-Hexamethyltetracosane (Squalane), and Diisodecyl Phthalate
Joback Method
KDB
Aqueous Solubility Prediction Method
Estimated Solubility Method
McGowan Method
NIST Webbook
The Yaws Handbook of Vapor Pressure
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