Chemical Properties of Diisodecyl phthalate (CAS 26761-40-0)

Diisodecyl phthalate

InChI
InChI=1S/C28H46O4/c1-23(2)17-11-7-5-9-15-21-31-27(29)25-19-13-14-20-26(25)28(30)32-22-16-10-6-8-12-18-24(3)4/h13-14,19-20,23-24H,5-12,15-18,21-22H2,1-4H3
InChI Key
ZVFDTKUVRCTHQE-UHFFFAOYSA-N
Formula
C28H46O4
SMILES
CC(C)CCCCCCCOC(=O)c1ccccc1C(=O)OCCCCCCCC(C)C
Molecular Weight1
446.67
CAS
26761-40-0
Other Names
  • 1,2-benzenedicarboxylic acid, diisodecyl ester
  • 3-methylnonyl 1,2-benzenedioate
  • bis(8-methylnonyl) benzene-1,2-dicarboxylate
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Contents

  1. Physical Properties
  2. Temperature Dependent Properties
  3. Datasets
  4. Correlations
  5. Similar Compounds
  6. Mixtures
  7. Sources

Physical Properties

Property Value Unit Source
ω 1.2313 Relay (1.0) Calculated Property
ΔfH°gas -1017.03 kJ/mol Relay (1.0) Calculated Property
ΔfusH° 63.62 kJ/mol Joback Calculated Property
ΔvapH° 121.21 kJ/mol Relay (1.0) Calculated Property
IE 9.39 eV Relay (1.0) Calculated Property
log10WS -7.99 Relay (1.0) Calculated Property
logPoct/wat 7.993 Crippen Calculated Property
McVol 396.500 ml/mol McGowan Calculated Property
Pc 787.27 kPa Joback Calculated Property
Tboil 686.66 K Relay (1.0) Calculated Property
Tc 889.09 K Relay (1.0) Calculated Property
Tfus 223.15 K Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Vc 1.487 m3/kmol Relay (1.0) Calculated Property

Cheméo can also estimate Standard Gibbs free energy of formation for this compound, but it falls outside the models' validated range, so it is not shown here. Open the prediction tool to compute it on demand.

Temperature Dependent Properties

Property Value Unit Temperature (K) Source
η [0.0049890; 0.6276000] Pa×s [273.15; 373.15] Show Hide
η 0.6276000 Pa×s 273.15 Temperature and Pressure Dependence of the Viscosity of Diisodecyl Phthalate at Temperatures between (0 and 100) deg C and at Pressures to 1 GPa
η 0.3935000 Pa×s 278.15 Temperature and Pressure Dependence of the Viscosity of Diisodecyl Phthalate at Temperatures between (0 and 100) deg C and at Pressures to 1 GPa
η 0.4046000 Pa×s 278.15 Study of the effects of pressure on the viscosity and density of diisodecyl phthalate
η 0.2648800 Pa×s 283.03 Viscosity Measurements of Diisodecyl Phthalate Using a Vibrating Wire Instrument Operated In Free Decay Mode: Comparison with Results Obtained with the Forced Mode of Operation
η 0.2656000 Pa×s 283.15 Viscosity of Diisodecyl Phthalate by Surface Light Scattering (SLS)
η 0.2612000 Pa×s 283.15 Study of the effects of pressure on the viscosity and density of diisodecyl phthalate
η 0.2552000 Pa×s 283.15 Temperature and Pressure Dependence of the Viscosity of Diisodecyl Phthalate at Temperatures between (0 and 100) deg C and at Pressures to 1 GPa
η 0.1759000 Pa×s 288.15 Study of the effects of pressure on the viscosity and density of diisodecyl phthalate
η 0.1774000 Pa×s 288.15 Viscosity of Diisodecyl Phthalate by Surface Light Scattering (SLS)
η 0.1709000 Pa×s 288.15 Temperature and Pressure Dependence of the Viscosity of Diisodecyl Phthalate at Temperatures between (0 and 100) deg C and at Pressures to 1 GPa
η 0.1763500 Pa×s 288.23 Viscosity Measurements of Diisodecyl Phthalate Using a Vibrating Wire Instrument Operated In Free Decay Mode: Comparison with Results Obtained with the Forced Mode of Operation
η 0.1739200 Pa×s 288.36 Viscosity Measurements of Diisodecyl Phthalate Using a Vibrating Wire Instrument Operated In Free Decay Mode: Comparison with Results Obtained with the Forced Mode of Operation
η 0.1223000 Pa×s 293.15 Study of the effects of pressure on the viscosity and density of diisodecyl phthalate
η 0.1238000 Pa×s 293.15 Viscosity of Diisodecyl Phthalate by Surface Light Scattering (SLS)
η 0.1226000 Pa×s 293.15 Temperature and Pressure Dependence of the Viscosity of Diisodecyl Phthalate at Temperatures between (0 and 100) deg C and at Pressures to 1 GPa
η 0.1233000 Pa×s 293.15 Densities, refractive indices, and viscosities of N,N-diethylethanol ammonium chloride - glycerol or - ethylene glycol deep eutectic solvents and their aqueous solutions
η 0.1223400 Pa×s 293.23 Viscosity Measurements of Diisodecyl Phthalate Using a Vibrating Wire Instrument Operated In Free Decay Mode: Comparison with Results Obtained with the Forced Mode of Operation
η 0.1165100 Pa×s 293.93 Viscosity Measurements of Diisodecyl Phthalate Using a Vibrating Wire Instrument Operated In Free Decay Mode: Comparison with Results Obtained with the Forced Mode of Operation
η 0.0877600 Pa×s 298.13 Viscosity Measurements of Diisodecyl Phthalate Using a Vibrating Wire Instrument Operated In Free Decay Mode: Comparison with Results Obtained with the Forced Mode of Operation
η 0.0884400 Pa×s 298.15 Viscosity of Diisodecyl Phthalate by Surface Light Scattering (SLS)
η 0.0883800 Pa×s 298.15 Densities, refractive indices, and viscosities of N,N-diethylethanol ammonium chloride - glycerol or - ethylene glycol deep eutectic solvents and their aqueous solutions
η 0.0877000 Pa×s 298.15 Temperature and Pressure Dependence of the Viscosity of Diisodecyl Phthalate at Temperatures between (0 and 100) deg C and at Pressures to 1 GPa
η 0.0841000 Pa×s 298.15 Temperature and Pressure Dependence of the Viscosity of Diisodecyl Phthalate at Temperatures between (0 and 100) deg C and at Pressures to 1 GPa
η 0.0872000 Pa×s 298.15 Density and Viscosity of Diisodecyl Phthalate C6H4(COOC10H21)2, with Nominal Viscosity at T ) 298 K and p ) 0.1 MPa of 87 mPaas, at Temperatures from (298.15 to 423.15) K and Pressures up to 70 MPa
η 0.0875200 Pa×s 298.15 Study of the effects of pressure on the viscosity and density of diisodecyl phthalate
η 0.0853000 Pa×s 298.58 Viscosity Measurements of Diisodecyl Phthalate Using a Vibrating Wire Instrument Operated In Free Decay Mode: Comparison with Results Obtained with the Forced Mode of Operation
η 0.0652400 Pa×s 303.15 Densities, refractive indices, and viscosities of N,N-diethylethanol ammonium chloride - glycerol or - ethylene glycol deep eutectic solvents and their aqueous solutions
η 0.0646000 Pa×s 303.15 Temperature and Pressure Dependence of the Viscosity of Diisodecyl Phthalate at Temperatures between (0 and 100) deg C and at Pressures to 1 GPa
η 0.0643100 Pa×s 303.15 Study of the effects of pressure on the viscosity and density of diisodecyl phthalate
η 0.0648400 Pa×s 303.15 Viscosity of Diisodecyl Phthalate by Surface Light Scattering (SLS)
η 0.0638000 Pa×s 303.15 Temperature and Pressure Dependence of the Viscosity of Diisodecyl Phthalate at Temperatures between (0 and 100) deg C and at Pressures to 1 GPa
η 0.0645100 Pa×s 303.18 Viscosity Measurements of Diisodecyl Phthalate Using a Vibrating Wire Instrument Operated In Free Decay Mode: Comparison with Results Obtained with the Forced Mode of Operation
η 0.0632500 Pa×s 303.50 Viscosity Measurements of Diisodecyl Phthalate Using a Vibrating Wire Instrument Operated In Free Decay Mode: Comparison with Results Obtained with the Forced Mode of Operation
η 0.0476000 Pa×s 308.15 Temperature and Pressure Dependence of the Viscosity of Diisodecyl Phthalate at Temperatures between (0 and 100) deg C and at Pressures to 1 GPa
η 0.0489800 Pa×s 308.15 Viscosity of Diisodecyl Phthalate by Surface Light Scattering (SLS)
η 0.0489000 Pa×s 308.15 Temperature and Pressure Dependence of the Viscosity of Diisodecyl Phthalate at Temperatures between (0 and 100) deg C and at Pressures to 1 GPa
η 0.0484600 Pa×s 308.15 Study of the effects of pressure on the viscosity and density of diisodecyl phthalate
η 0.0380100 Pa×s 313.15 Viscosity of Diisodecyl Phthalate by Surface Light Scattering (SLS)
η 0.0366000 Pa×s 313.15 Temperature and Pressure Dependence of the Viscosity of Diisodecyl Phthalate at Temperatures between (0 and 100) deg C and at Pressures to 1 GPa
η 0.0378500 Pa×s 313.15 Densities, refractive indices, and viscosities of N,N-diethylethanol ammonium chloride - glycerol or - ethylene glycol deep eutectic solvents and their aqueous solutions
η 0.0373500 Pa×s 313.15 Study of the effects of pressure on the viscosity and density of diisodecyl phthalate
η 0.0293800 Pa×s 318.15 Study of the effects of pressure on the viscosity and density of diisodecyl phthalate
η 0.0237300 Pa×s 323.15 Densities, refractive indices, and viscosities of N,N-diethylethanol ammonium chloride - glycerol or - ethylene glycol deep eutectic solvents and their aqueous solutions
η 0.0235100 Pa×s 323.15 Study of the effects of pressure on the viscosity and density of diisodecyl phthalate
η 0.0238500 Pa×s 323.15 Density and Viscosity of Diisodecyl Phthalate C6H4(COOC10H21)2, with Nominal Viscosity at T ) 298 K and p ) 0.1 MPa of 87 mPaas, at Temperatures from (298.15 to 423.15) K and Pressures up to 70 MPa
η 0.0230000 Pa×s 323.15 Temperature and Pressure Dependence of the Viscosity of Diisodecyl Phthalate at Temperatures between (0 and 100) deg C and at Pressures to 1 GPa
η 0.0191300 Pa×s 328.15 Study of the effects of pressure on the viscosity and density of diisodecyl phthalate
η 0.0160300 Pa×s 333.15 Densities, refractive indices, and viscosities of N,N-diethylethanol ammonium chloride - glycerol or - ethylene glycol deep eutectic solvents and their aqueous solutions
η 0.0155000 Pa×s 333.15 Temperature and Pressure Dependence of the Viscosity of Diisodecyl Phthalate at Temperatures between (0 and 100) deg C and at Pressures to 1 GPa
η 0.0157900 Pa×s 333.15 Study of the effects of pressure on the viscosity and density of diisodecyl phthalate
η 0.0132100 Pa×s 338.15 Study of the effects of pressure on the viscosity and density of diisodecyl phthalate
η 0.0110000 Pa×s 343.15 Temperature and Pressure Dependence of the Viscosity of Diisodecyl Phthalate at Temperatures between (0 and 100) deg C and at Pressures to 1 GPa
η 0.0113100 Pa×s 343.15 Densities, refractive indices, and viscosities of N,N-diethylethanol ammonium chloride - glycerol or - ethylene glycol deep eutectic solvents and their aqueous solutions
η 0.0111800 Pa×s 343.15 Study of the effects of pressure on the viscosity and density of diisodecyl phthalate
η 0.0097100 Pa×s 348.15 Density and Viscosity of Diisodecyl Phthalate C6H4(COOC10H21)2, with Nominal Viscosity at T ) 298 K and p ) 0.1 MPa of 87 mPaas, at Temperatures from (298.15 to 423.15) K and Pressures up to 70 MPa
η 0.0095610 Pa×s 348.15 Study of the effects of pressure on the viscosity and density of diisodecyl phthalate
η 0.0081200 Pa×s 353.15 Temperature and Pressure Dependence of the Viscosity of Diisodecyl Phthalate at Temperatures between (0 and 100) deg C and at Pressures to 1 GPa
η 0.0082570 Pa×s 353.15 Study of the effects of pressure on the viscosity and density of diisodecyl phthalate
η 0.0071930 Pa×s 358.15 Study of the effects of pressure on the viscosity and density of diisodecyl phthalate
η 0.0063900 Pa×s 363.15 Density and Viscosity of Diisodecyl Phthalate C6H4(COOC10H21)2, with Nominal Viscosity at T ) 298 K and p ) 0.1 MPa of 87 mPaas, at Temperatures from (298.15 to 423.15) K and Pressures up to 70 MPa
η 0.0063290 Pa×s 363.15 Study of the effects of pressure on the viscosity and density of diisodecyl phthalate
η 0.0056020 Pa×s 368.15 Study of the effects of pressure on the viscosity and density of diisodecyl phthalate
η 0.0049890 Pa×s 373.15 Study of the effects of pressure on the viscosity and density of diisodecyl phthalate
n0 1.48450 293.15 New Measurements of the Viscosity of Diisodecyl Phthalate Using a Vibrating Wire Technique
ρl [881.29; 980.22] kg/m3 [273.84; 413.33] Show Hide
ρl 980.22 kg/m3 273.84 Thermodynamic properties and equation of state of liquid di-isodecyl phthalate at temperature between (273 and 423) K and at pressures up to 140 MPa
ρl 980.07 kg/m3 274.06 Thermodynamic properties and equation of state of liquid di-isodecyl phthalate at temperature between (273 and 423) K and at pressures up to 140 MPa
ρl 980.08 kg/m3 274.07 Thermodynamic properties and equation of state of liquid di-isodecyl phthalate at temperature between (273 and 423) K and at pressures up to 140 MPa
ρl 979.86 kg/m3 274.35 Thermodynamic properties and equation of state of liquid di-isodecyl phthalate at temperature between (273 and 423) K and at pressures up to 140 MPa
ρl 973.75 kg/m3 282.95 Thermodynamic properties and equation of state of liquid di-isodecyl phthalate at temperature between (273 and 423) K and at pressures up to 140 MPa
ρl 962.88 kg/m3 298.25 Thermodynamic properties and equation of state of liquid di-isodecyl phthalate at temperature between (273 and 423) K and at pressures up to 140 MPa
ρl 962.83 kg/m3 298.28 Thermodynamic properties and equation of state of liquid di-isodecyl phthalate at temperature between (273 and 423) K and at pressures up to 140 MPa
ρl 957.83 kg/m3 305.26 Thermodynamic properties and equation of state of liquid di-isodecyl phthalate at temperature between (273 and 423) K and at pressures up to 140 MPa
ρl 952.21 kg/m3 313.27 Thermodynamic properties and equation of state of liquid di-isodecyl phthalate at temperature between (273 and 423) K and at pressures up to 140 MPa
ρl 952.15 kg/m3 313.27 Thermodynamic properties and equation of state of liquid di-isodecyl phthalate at temperature between (273 and 423) K and at pressures up to 140 MPa
ρl 937.93 kg/m3 333.28 Thermodynamic properties and equation of state of liquid di-isodecyl phthalate at temperature between (273 and 423) K and at pressures up to 140 MPa
ρl 923.76 kg/m3 353.29 Thermodynamic properties and equation of state of liquid di-isodecyl phthalate at temperature between (273 and 423) K and at pressures up to 140 MPa
ρl 909.62 kg/m3 373.29 Thermodynamic properties and equation of state of liquid di-isodecyl phthalate at temperature between (273 and 423) K and at pressures up to 140 MPa
ρl 895.47 kg/m3 393.31 Thermodynamic properties and equation of state of liquid di-isodecyl phthalate at temperature between (273 and 423) K and at pressures up to 140 MPa
ρl 881.29 kg/m3 413.33 Thermodynamic properties and equation of state of liquid di-isodecyl phthalate at temperature between (273 and 423) K and at pressures up to 140 MPa
γ [0.03; 0.03] N/m [288.15; 308.15] Show Hide
γ 0.03 N/m 288.15 Diisodecylphthalate (DIDP)-a potential standard of moderate viscosity: Surface tension measurements and water content effect on viscosity
γ 0.03 N/m 293.15 Diisodecylphthalate (DIDP)-a potential standard of moderate viscosity: Surface tension measurements and water content effect on viscosity
γ 0.03 N/m 298.15 Diisodecylphthalate (DIDP)-a potential standard of moderate viscosity: Surface tension measurements and water content effect on viscosity
γ 0.03 N/m 303.15 Diisodecylphthalate (DIDP)-a potential standard of moderate viscosity: Surface tension measurements and water content effect on viscosity
γ 0.03 N/m 308.15 Diisodecylphthalate (DIDP)-a potential standard of moderate viscosity: Surface tension measurements and water content effect on viscosity

Datasets

  1. Viscosity, Pa*s (3)
  2. Mass density, kg/m3 (1)

Viscosity, Pa*s

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Viscosity, Pa*s - Liquid
298.15 200.00 0.0876
298.15 10000.00 0.1121
298.15 20000.00 0.1434
298.15 40000.00 0.2309
298.15 200.00 0.0876
298.15 10000.00 0.1121
298.15 20000.00 0.1434
298.15 40000.00 0.2310
298.15 200.00 0.0876
298.15 10000.00 0.1123
298.15 20000.00 0.1437
298.15 40000.00 0.2311
298.15 200.00 0.0876
298.15 40000.00 0.2314
298.15 200.00 0.0876
298.15 40000.00 0.2316
298.15 200.00 0.0876
298.15 40000.00 0.2316
298.15 200.00 0.0877
298.15 200.00 0.0876
298.15 200.00 0.0877
298.15 200.00 0.0877
305.15 200.00 0.0570
305.15 200.00 0.0571
305.15 200.00 0.0571
305.15 200.00 0.0571
305.15 200.00 0.0572
313.15 200.00 0.0374
313.15 10100.00 0.0463
313.15 20000.00 0.0573
313.15 40000.00 0.0872
313.15 59900.00 0.1305
313.15 60000.00 0.1303
313.15 80000.00 0.1941
313.15 200.00 0.0374
313.15 10100.00 0.0463
313.15 20000.00 0.0573
313.15 40000.00 0.0871
313.15 59900.00 0.1303
313.15 80000.00 0.1944
313.15 200.00 0.0373
313.15 10100.00 0.0462
313.15 20000.00 0.0573
313.15 40000.00 0.0870
313.15 80000.00 0.1952
313.15 200.00 0.0371
313.15 200.00 0.0371
313.15 200.00 0.0371
343.15 200.00 0.0112
343.15 10100.00 0.0133
343.15 20100.00 0.0158
343.15 40000.00 0.0220
343.15 80100.00 0.0412
343.15 137100.00 0.0956
343.15 200.00 0.0112
343.15 10100.00 0.0133
343.15 20100.00 0.0159
343.15 40000.00 0.0221
343.15 80100.00 0.0412
343.15 137100.00 0.0956
343.15 200.00 0.0112
343.15 10100.00 0.0134
343.15 20100.00 0.0159
343.15 40000.00 0.0221
343.15 80100.00 0.0412
343.15 137100.00 0.0956
343.15 200.00 0.0110
343.15 200.00 0.0110
343.15 200.00 0.0110
368.15 300.00 0.0056
368.15 300.00 0.0056
368.15 300.00 0.0056
368.15 300.00 0.0056
373.15 300.00 0.0050
373.15 20100.00 0.0069
373.15 40000.00 0.0091
373.15 80100.00 0.0152
373.15 137200.00 0.0301
373.15 300.00 0.0050
373.15 20100.00 0.0069
373.15 40000.00 0.0091
373.15 80100.00 0.0152
373.15 137200.00 0.0301
373.15 300.00 0.0050
373.15 20100.00 0.0069
373.15 40000.00 0.0091
373.15 80100.00 0.0152
373.15 137200.00 0.0301
373.15 300.00 0.0049
373.15 300.00 0.0049
373.15 300.00 0.0049
Reference
Fixed Measured
Pressure, kPa - Liquid Temperature, K - Liquid Viscosity, Pa*s - Liquid
2460.00 302.75 0.0704
2460.00 302.75 0.0706
2450.00 302.75 0.0701
4510.00 302.75 0.0740
4510.00 302.75 0.0740
6440.00 302.75 0.0773
6440.00 302.75 0.0776
8390.00 302.75 0.0811
10250.00 302.75 0.0850
10250.00 302.75 0.0853
11190.00 302.75 0.0872
13300.00 302.75 0.0922
15370.00 302.75 0.0963
17310.00 302.75 0.1013
2430.00 342.69 0.0118
2430.00 342.69 0.0118
2420.00 342.69 0.0119
4260.00 342.69 0.0121
6130.00 342.69 0.0125
7970.00 342.67 0.0131
7970.00 342.67 0.0130
9700.00 342.67 0.0134
9700.00 342.67 0.0134
10950.00 342.90 0.0137
10970.00 342.90 0.0137
13180.00 342.90 0.0143
13180.00 342.90 0.0143
15220.00 342.90 0.0147
15220.00 342.90 0.0147
17130.00 342.94 0.0151
Reference
Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Viscosity, Pa*s - Liquid
273.15 100.00 0.6258
273.15 9900.00 0.8451
298.15 100.00 0.0874
298.15 9600.00 0.1107
298.15 20600.00 0.1450
298.15 20700.00 0.1455
298.15 30100.00 0.1825
298.15 30300.00 0.1830
298.15 40700.00 0.2342
298.15 50200.00 0.2894
298.15 59200.00 0.3562
298.15 71600.00 0.4654
298.15 82000.00 0.5890
298.15 83300.00 0.6084
298.15 100.00 0.0874
313.15 100.00 0.0377
313.15 10900.00 0.0473
313.15 21200.00 0.0590
313.15 30600.00 0.0715
313.15 40900.00 0.0890
313.15 51600.00 0.1091
313.15 62400.00 0.1367
313.15 71300.00 0.1608
313.15 80300.00 0.1924
313.15 89800.00 0.2344
338.15 100.00 0.0131
338.15 9700.00 0.0155
338.15 10700.00 0.0163
338.15 19400.00 0.0186
338.15 20500.00 0.0194
338.15 31000.00 0.0233
338.15 31770.00 0.0230
338.15 40100.00 0.0272
338.15 41110.00 0.0269
338.15 50300.00 0.0324
338.15 51100.00 0.0319
338.15 60400.00 0.0383
338.15 60510.00 0.0373
338.15 70700.00 0.0452
338.15 70710.00 0.0436
338.15 80200.00 0.0525
338.15 80970.00 0.0517
338.15 100.00 0.0134
338.15 100.00 0.0134
338.15 100.00 0.0134
348.15 100.00 0.0097
348.15 9800.00 0.0115
348.15 20600.00 0.0137
348.15 30230.00 0.0160
348.15 31300.00 0.0163
348.15 40810.00 0.0189
348.15 50600.00 0.0221
348.15 50710.00 0.0221
348.15 61220.00 0.0259
348.15 69800.00 0.0298
348.15 72330.00 0.0306
348.15 85770.00 0.0372
Reference

Mass density, kg/m3

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mass density, kg/m3 - Liquid
283.15 100.00 974.5
283.15 200.00 974.5
283.15 400.00 974.6
283.15 600.00 974.7
283.15 800.00 974.9
283.15 1010.00 975.0
283.15 2000.00 975.5
283.15 3020.00 976.0
283.15 4000.00 976.6
283.15 5000.00 977.1
283.15 6000.00 977.7
283.15 6980.00 978.2
283.15 8010.00 978.7
283.15 9020.00 979.3
283.15 10030.00 979.8
283.15 15000.00 982.4
283.15 19970.00 985.0
283.15 25030.00 987.3
283.15 29980.00 989.8
283.15 35030.00 992.1
283.15 40000.00 994.5
283.15 45030.00 996.6
283.15 49980.00 998.8
283.15 55030.00 1000.9
283.15 59990.00 1002.6
283.15 64990.00 1005.1
288.15 100.00 970.7
288.15 200.00 970.8
288.15 420.00 970.9
288.15 600.00 971.0
288.15 790.00 971.1
288.15 1000.00 971.2
288.15 1990.00 971.7
288.15 3020.00 972.3
288.15 4010.00 972.9
288.15 5000.00 973.4
288.15 6010.00 974.0
288.15 7020.00 974.5
288.15 7980.00 975.0
288.15 9000.00 975.5
288.15 10000.00 976.1
288.15 14990.00 978.7
288.15 19970.00 981.4
288.15 25000.00 983.8
288.15 30000.00 986.4
288.15 34990.00 988.8
288.15 40020.00 991.1
288.15 45000.00 993.3
288.15 49980.00 995.7
288.15 54980.00 997.7
288.15 60000.00 999.9
288.15 65000.00 1002.0
293.15 100.00 967.0
293.15 200.00 967.1
293.15 400.00 967.2
293.15 630.00 967.3
293.15 790.00 967.4
293.15 1000.00 967.5
293.15 2010.00 968.1
293.15 3020.00 968.7
293.15 4020.00 969.2
293.15 4970.00 969.8
293.15 5980.00 970.3
293.15 7020.00 970.9
293.15 8000.00 971.5
293.15 9020.00 972.0
293.15 10010.00 972.6
293.15 15010.00 975.2
293.15 20000.00 977.9
293.15 25030.00 980.5
293.15 30020.00 983.0
293.15 35030.00 985.4
293.15 40010.00 987.8
293.15 44980.00 990.1
293.15 50020.00 992.4
293.15 55020.00 994.6
293.15 60020.00 996.8
293.15 65000.00 998.9
298.15 100.00 963.4
298.15 200.00 963.4
298.15 410.00 963.6
298.15 620.00 963.7
298.15 820.00 963.8
298.15 1000.00 963.9
298.15 2020.00 964.5
298.15 3040.00 965.0
298.15 4030.00 965.7
298.15 4980.00 966.2
298.15 6070.00 966.8
298.15 7020.00 967.3
298.15 8040.00 967.9
298.15 9040.00 968.5
298.15 10030.00 969.0
298.15 15010.00 971.7
298.15 19990.00 974.4
298.15 25000.00 977.0
298.15 30020.00 979.6
298.15 35000.00 982.1
298.15 40020.00 984.5
298.15 44970.00 986.9
298.15 49990.00 989.2
298.15 54970.00 991.4
298.15 60000.00 993.7
298.15 65020.00 995.8
303.15 100.00 959.7
303.15 200.00 959.8
303.15 400.00 959.9
303.15 580.00 960.0
303.15 800.00 960.2
303.15 1000.00 960.3
303.15 2000.00 960.9
303.15 2990.00 961.4
303.15 4000.00 962.0
303.15 5000.00 962.6
303.15 6000.00 963.2
303.15 7000.00 963.8
303.15 7980.00 964.3
303.15 9000.00 964.9
303.15 10020.00 965.5
303.15 14970.00 968.2
303.15 20010.00 971.0
303.15 25030.00 973.6
303.15 30020.00 976.3
303.15 35000.00 978.8
303.15 40000.00 981.2
303.15 45000.00 983.6
303.15 50010.00 986.0
303.15 54980.00 988.3
303.15 60000.00 990.5
303.15 64990.00 992.7
308.15 100.00 956.2
308.15 200.00 956.2
308.15 410.00 956.4
308.15 610.00 956.5
308.15 800.00 956.6
308.15 1000.00 956.7
308.15 2010.00 957.3
308.15 3020.00 957.9
308.15 4000.00 958.5
308.15 5000.00 959.1
308.15 6000.00 959.7
308.15 7020.00 960.3
308.15 8000.00 960.8
308.15 9020.00 961.4
308.15 10000.00 962.0
308.15 15010.00 964.8
308.15 19990.00 967.6
308.15 25000.00 970.3
308.15 30010.00 973.0
308.15 35000.00 975.5
308.15 39990.00 978.0
308.15 44990.00 980.4
308.15 50010.00 982.9
308.15 55000.00 985.2
308.15 60000.00 987.4
308.15 65000.00 989.7
313.15 100.00 952.6
313.15 200.00 952.6
313.15 400.00 952.8
313.15 620.00 952.9
313.15 800.00 953.0
313.15 1030.00 953.1
313.15 2010.00 953.7
313.15 3000.00 954.3
313.15 4000.00 955.0
313.15 5020.00 955.5
313.15 5990.00 956.2
313.15 7030.00 956.7
313.15 8000.00 957.4
313.15 9020.00 957.9
313.15 10010.00 958.5
313.15 15010.00 961.4
313.15 20000.00 964.2
313.15 25030.00 967.0
313.15 30000.00 969.7
313.15 35020.00 972.2
313.15 40020.00 974.8
313.15 45010.00 977.2
313.15 49970.00 979.7
313.15 55000.00 982.0
313.15 59980.00 984.4
313.15 64970.00 986.6
323.15 100.00 945.4
323.15 210.00 945.5
323.15 400.00 945.6
323.15 600.00 945.7
323.15 800.00 945.9
323.15 1000.00 946.0
323.15 2000.00 946.6
323.15 3030.00 947.2
323.15 4030.00 947.9
323.15 5020.00 948.5
323.15 6010.00 949.1
323.15 7000.00 949.7
323.15 8000.00 950.3
323.15 9010.00 950.9
323.15 10020.00 951.6
323.15 15000.00 954.5
323.15 20010.00 957.5
323.15 25030.00 960.3
323.15 30010.00 963.2
323.15 34970.00 965.8
323.15 40000.00 968.5
323.15 45000.00 970.9
323.15 49980.00 973.5
323.15 54980.00 975.8
323.15 60000.00 978.3
323.15 65000.00 980.6
333.15 100.00 938.3
333.15 200.00 938.4
333.15 400.00 938.5
333.15 630.00 938.7
333.15 800.00 938.8
333.15 1000.00 938.9
333.15 2010.00 939.6
333.15 3000.00 940.2
333.15 4000.00 940.9
333.15 5000.00 941.5
333.15 6000.00 942.2
333.15 7030.00 942.8
333.15 7980.00 943.5
333.15 9010.00 944.1
333.15 10030.00 944.8
333.15 14990.00 947.9
333.15 20000.00 951.0
333.15 25000.00 953.8
333.15 30020.00 956.7
333.15 34990.00 959.4
333.15 39970.00 962.2
333.15 45020.00 964.8
333.15 50000.00 967.4
333.15 55020.00 969.8
333.15 60000.00 972.3
333.15 65000.00 974.7
343.15 100.00 931.2
343.15 220.00 931.3
343.15 430.00 931.5
343.15 610.00 931.6
343.15 810.00 931.8
343.15 1000.00 931.9
343.15 2000.00 932.6
343.15 3000.00 933.3
343.15 3980.00 934.0
343.15 5010.00 934.6
343.15 5980.00 935.3
343.15 7000.00 936.0
343.15 7990.00 936.6
343.15 9020.00 937.3
343.15 9980.00 937.9
343.15 15010.00 941.2
343.15 19990.00 944.3
343.15 25010.00 947.4
343.15 29980.00 950.4
343.15 35030.00 953.3
343.15 40030.00 956.1
343.15 45010.00 958.7
343.15 50050.00 961.4
343.15 55000.00 964.0
343.15 60000.00 966.5
343.15 65020.00 968.9
353.15 100.00 924.2
353.15 200.00 924.3
353.15 410.00 924.5
353.15 630.00 924.6
353.15 800.00 924.8
353.15 1010.00 924.9
353.15 2000.00 925.6
353.15 3000.00 926.3
353.15 3980.00 927.0
353.15 4990.00 927.7
353.15 6000.00 928.4
353.15 7000.00 929.1
353.15 8010.00 929.8
353.15 9000.00 930.5
353.15 10010.00 931.2
353.15 15040.00 934.6
353.15 20000.00 937.9
353.15 24970.00 941.0
353.15 29980.00 944.1
353.15 35010.00 947.1
353.15 40000.00 950.0
353.15 45000.00 952.7
353.15 49990.00 955.5
353.15 55000.00 958.1
353.15 60010.00 960.7
353.15 65020.00 963.2
363.15 100.00 917.2
363.15 200.00 917.3
363.15 420.00 917.4
363.15 600.00 917.6
363.15 800.00 917.7
363.15 990.00 917.9
363.15 2000.00 918.6
363.15 2980.00 919.4
363.15 3960.00 920.1
363.15 4970.00 920.9
363.15 5990.00 921.6
363.15 7020.00 922.3
363.15 7980.00 923.0
363.15 9030.00 923.8
363.15 10000.00 924.5
363.15 15000.00 928.0
363.15 19990.00 931.4
363.15 25010.00 934.7
363.15 30020.00 937.9
363.15 34980.00 940.9
363.15 39990.00 943.9
363.15 44980.00 946.8
363.15 49990.00 949.6
363.15 55000.00 952.3
363.15 60040.00 955.0
363.15 64990.00 957.6
Reference

Correlations

Property Value Unit Temperature (K) Source
Cp,gas [576.81; 1359.60] J/mol×K [273.00; 1000.00] Joback Predicted correlation Show Hide
EquationY = A + B·T + C·T² + D·T³ + E·T⁴
Y is Cp,gas in J/mol×K, T in K
Coefficient A5.28400e+00
Coefficient B2.42768e+00
Coefficient C-1.28076e-03
Coefficient D2.07400e-07
Coefficient E0.00000e+00
Temperature range, min.273.00
Temperature range, max.1000.00
Cp,gas 576.81 J/mol×K 273.00 Calculated Property
Cp,gas 713.03 J/mol×K 353.78 Calculated Property
Cp,gas 835.41 J/mol×K 434.56 Calculated Property
Cp,gas 944.60 J/mol×K 515.33 Calculated Property
Cp,gas 1041.27 J/mol×K 596.11 Calculated Property
Cp,gas 1126.06 J/mol×K 676.89 Calculated Property
Cp,gas 1199.63 J/mol×K 757.67 Calculated Property
Cp,gas 1262.64 J/mol×K 838.44 Calculated Property
Cp,gas 1315.75 J/mol×K 919.22 Calculated Property
Cp,gas 1359.60 J/mol×K 1000.00 Calculated Property
Property Value Unit Temperature (K) Source
Pvap [1.07e-12; 103.45] kPa [233.00; 723.00] KDB Vapor Pressure Data Show Hide
Equationln(Y) = A + B/T + C·ln(T) + D·T² + E/T²
Y is Pvap in kPa, T in K
Coefficient A1.24183e+02
Coefficient B-1.55755e+04
Coefficient C-1.56745e+01
Coefficient D9.93021e-06
Coefficient E0.00000e+00
Temperature range, min.233.00
Temperature range, max.723.00
Pvap 1.07e-12 kPa 233.00 Calculated Property
Pvap 1.66e-08 kPa 287.44 Calculated Property
Pvap 8.58e-06 kPa 341.89 Calculated Property
Pvap 6.59e-04 kPa 396.33 Calculated Property
Pvap 0.02 kPa 450.78 Calculated Property
Pvap 0.19 kPa 505.22 Calculated Property
Pvap 1.33 kPa 559.67 Calculated Property
Pvap 6.90 kPa 614.11 Calculated Property
Pvap 28.78 kPa 668.56 Calculated Property
Pvap 103.45 kPa 723.00 Calculated Property

Similar Compounds

Isooctyl decyl phthalate. Diisononyl phthalate. 1,2-Benzenedicarboxylic acid, butyl 8-methylnonyl ester. 1,2-Benzenedicarboxylic acid, bis(6-methylheptyl) ester. Phthalic acid, di(4-methylpentyl) ester. 1,2-Benzenedicarboxylic acid, bis(4-methylpentyl) ester. Phthalic acid, dodecyl 3-methylbutyl ester. Phthalic acid, 3-methylbutyl undecyl ester. Phthalic acid, 3-methylbutyl octyl ester. Phthalic acid, 3-methylbutyl octadecyl ester. Phthalic acid, hexadecyl 3-methylbutyl ester. Phthalic acid, 3-methylbutyl tetradecyl ester. Phthalic acid, heptadecyl 3-methylbutyl ester. Phthalic acid, 3-methylbutyl nonyl ester. Phthalic acid, 3-methylbutyl tridecyl ester.

Find more compounds similar to Diisodecyl phthalate.

Mixtures

Sources

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