Chemical Properties of Bis(2-ethylhexyl) phthalate (CAS 117-81-7)

InChI

InChI=1S/C24H38O4/c1-5-9-13-19(7-3)17-27-23(25)21-15-11-12-16-22(21)24(26)28-18-20(8-4)14-10-6-2/h11-12,15-16,19-20H,5-10,13-14,17-18H2,1-4H3

InChI Key

BJQHLKABXJIVAM-UHFFFAOYSA-N

Formula

C24H38O4

SMILES

CCCCC(CC)COC(=O)c1ccccc1C(=O)OCC(CC)CCCC

Molecular Weight¹

390.56

CAS

117-81-7

Other Names

• 1,2-Benzenedicarboxylic acid, 1,2-bis(2-ethylhexyl) ester
• 1,2-benzenedicarboxylic acid, bis(2-ethylhexyl) ester
• 2-Ethylhexyl phthalate
• BEHP
• BIS (2-ETHYLHEXYL) PHTHALATE
• Bis(2-ethylhexyl)ester phthalic acid
• Bis-(2-ethylhexyl)ester kyseliny ftalove
• Bis-(2-ethylhexyl)ester kyseliny ftalove (Czech)
• Celluflex DOP
• Compound 889
• Corflex 400
• DAF 68
• DEHP
• DIOCTYL PHTHALATE
• DOF
• DOP
• Di(2-ethylhexyl) o-phthalate
• Di(2-ethylhexyl)-phthalate
• Di(2-ethylhexyl)orthophthalate
• Di(ethylhexyl) phthalate
• Di-sec-octyl phthalate
• Ergoplast FDO-S
• Ethylhexyl phthalate
• Eviplast 80
• Eviplast 81
• Fleximel
• Flexol plasticizer DOP
• Good-rite GP 264
• Hatco DOP
• Hatcol dop
• Hercoflex 260
• Jayflex DOP
• Kodaflex DOP
• Merrol DOP
• Mollan O
• NCI-C52733
• Nuoplaz DOP
• Octyl phthalate
• PX-138
• Palatinol AH
• Palatinol AH-L
• Palatinol DOP
• Phthalic acid dioctyl ester
• Pittsburgh PX-138
• Plasthall DOP
• Platinol AH
• Platinol DOP
• Polycizer DOP
• RC plasticizer DOP
• RCRA Waste number U028
• Reomol D 79P
• Reomol DOP
• Sansocizer DOP
• Sicol 150
• Staflex DOP
• Truflex DOP
• Union carbide flexol 380
• Vestinol AH
• Vinycizer 80
• Witcizer 312
• bis(2-ethylhexyl) 1,2-benzenedicarboxylate
• bis(2-ethylhexyl) benzene-1,2-dicarboxylate
• bis(2-ethylhexyl) o-phthalate
• bisoflex 81
• bisoflex DOP
• di(2-ethylhexyl) phthalate
• ergoplast FDO
• etalon
• flexol DOP
• monocizer DOP
• octoil
• phthalic acid di(2-ethylhexyl) ester
• phthalic acid, bis(2-ethylhexyl) ester
• sconamoll DOP
• vinicizer 80

• ω : Acentric Factor.
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• η : Dynamic viscosity (Pa×s).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• D^*_i : Self diffusion coefficient (m²/s).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• V_c : Critical Volume (m³/kmol).
• ¹: Molecular weight from the IUPAC atomic weights tables.

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	1.0404		Relay (1.0) Calculated Property
ΔfH°gas	-933.86	kJ/mol	Relay (1.0) Calculated Property
ΔfusH°	53.26	kJ/mol	Joback Calculated Property
ΔvapH°	106.14	kJ/mol	Relay (1.0) Calculated Property
log10WS	[-7.06; -6.96]
log10WS	-7.06		Aq. Solubility Prediction
log10WS	-6.96		Estimated Solubility
logPoct/wat	6.433		Crippen Calculated Property
McVol	340.140	ml/mol	McGowan Calculated Property
Pc	1070.00	kPa	Critical Temperatures and Pressures of 12 Phthalates Using the Pulse-Heating Method
Inp	[402.20; 2552.00]
Inp	2488.00		NIST
Inp	2505.00		NIST
Inp	2492.60		NIST
Inp	Outlier 418.60		NIST
Inp	2492.60		NIST
Inp	2509.00		NIST
Inp	2507.00		NIST
Inp	2499.40		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	2509.00		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	Outlier 406.14		NIST
Inp	2539.00		NIST
Inp	2519.00		NIST
Inp	2499.40		NIST
Inp	2507.00		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	862.41	K	Relay (1.0) Calculated Property
Tfus	219.82	K	Aq. Solubility Prediction
Vc	1.243	m3/kmol	Relay (1.0) Calculated Property

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

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
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	Measurements of the Viscosity of Bis(2-ethylhexyl) Sebacate, Squalane, and Bis(2-ethylhexyl) Phthalate between (283 and 363) K at 0.1 MPa
η	0.0787300	Pa×s	293.38	Measurements of the Viscosity of Bis(2-ethylhexyl) Sebacate, Squalane, and Bis(2-ethylhexyl) Phthalate between (283 and 363) K at 0.1 MPa
η	0.0579400	Pa×s	298.29	Measurements of the Viscosity of Bis(2-ethylhexyl) Sebacate, Squalane, and Bis(2-ethylhexyl) Phthalate between (283 and 363) K at 0.1 MPa
η	0.0432700	Pa×s	303.33	Measurements of the Viscosity of Bis(2-ethylhexyl) Sebacate, Squalane, and Bis(2-ethylhexyl) Phthalate between (283 and 363) K at 0.1 MPa
η	0.0331700	Pa×s	308.23	Measurements of the Viscosity of Bis(2-ethylhexyl) Sebacate, Squalane, and Bis(2-ethylhexyl) Phthalate between (283 and 363) K at 0.1 MPa
η	0.0261300	Pa×s	313.18	Measurements of the Viscosity of Bis(2-ethylhexyl) Sebacate, Squalane, and Bis(2-ethylhexyl) Phthalate between (283 and 363) K at 0.1 MPa
η	0.0210800	Pa×s	317.99	Measurements of the Viscosity of Bis(2-ethylhexyl) Sebacate, Squalane, and Bis(2-ethylhexyl) Phthalate between (283 and 363) K at 0.1 MPa
η	0.0169600	Pa×s	323.02	Measurements of the Viscosity of Bis(2-ethylhexyl) Sebacate, Squalane, and Bis(2-ethylhexyl) Phthalate between (283 and 363) K at 0.1 MPa
η	0.0139100	Pa×s	328.12	Measurements of the Viscosity of Bis(2-ethylhexyl) Sebacate, Squalane, and Bis(2-ethylhexyl) Phthalate between (283 and 363) K at 0.1 MPa
η	0.0116200	Pa×s	333.19	Measurements of the Viscosity of Bis(2-ethylhexyl) Sebacate, Squalane, and Bis(2-ethylhexyl) Phthalate between (283 and 363) K at 0.1 MPa
η	0.0099030	Pa×s	337.71	Measurements of the Viscosity of Bis(2-ethylhexyl) Sebacate, Squalane, and Bis(2-ethylhexyl) Phthalate between (283 and 363) K at 0.1 MPa
η	0.0082680	Pa×s	343.53	Measurements of the Viscosity of Bis(2-ethylhexyl) Sebacate, Squalane, and Bis(2-ethylhexyl) Phthalate between (283 and 363) K at 0.1 MPa
η	0.0071580	Pa×s	348.48	Measurements of the Viscosity of Bis(2-ethylhexyl) Sebacate, Squalane, and Bis(2-ethylhexyl) Phthalate between (283 and 363) K at 0.1 MPa
η	0.0061990	Pa×s	353.68	Measurements of the Viscosity of Bis(2-ethylhexyl) Sebacate, Squalane, and Bis(2-ethylhexyl) Phthalate between (283 and 363) K at 0.1 MPa
ΔvapH	[102.50; 116.90]	kJ/mol	[298.00; 516.50]
ΔvapH	116.90	kJ/mol	298.00	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
ΔvapH	110.70	kJ/mol	412.50	NIST
ΔvapH	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 Pressure and Enthalpy of Vaporization of Fentanyl
Pvap	0.02	kPa	433.15	Vapor Pressure and Enthalpy of Vaporization of Fentanyl
Pvap	0.03	kPa	443.15	Vapor Pressure and Enthalpy of Vaporization of Fentanyl
Pvap	0.04	kPa	448.15	Vapor Pressure and Enthalpy of Vaporization of Fentanyl
Pvap	0.07	kPa	453.15	Vapor Pressure and Enthalpy of Vaporization of Fentanyl
Pvap	0.12	kPa	463.15	Vapor Pressure and Enthalpy of Vaporization of Fentanyl
Pvap	0.19	kPa	473.15	Vapor Pressure and Enthalpy of Vaporization of Fentanyl
ρl	[931.85; 998.82]	kg/m3	[273.15; 363.15]
ρl	998.82	kg/m3	273.15	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
ρl	995.01	kg/m3	278.15	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
ρl	991.26	kg/m3	283.15	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
ρl	983.87	kg/m3	293.15	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
ρl	980.15	kg/m3	298.15	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
ρl	976.42	kg/m3	303.15	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
ρl	968.98	kg/m3	313.15	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
ρl	961.53	kg/m3	323.15	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
ρl	954.11	kg/m3	333.15	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
ρl	946.68	kg/m3	343.15	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
ρl	939.27	kg/m3	353.15	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
ρl	931.85	kg/m3	363.15	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
D*i	[0.00; 0.00]	m2/s	[303.18; 362.75]
D*i	0.00	m2/s	303.18	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	312.89	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	322.70	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	322.84	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	322.88	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	323.03	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	323.05	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	333.16	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	333.20	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	343.65	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	343.70	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	352.86	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	352.88	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	362.72	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	362.75	Viscous Calibration Liquids for Self-diffusion Measurements

Datasets

1. Molar heat capacity at constant pressure, J/K/mol (1)
2. 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

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[491.95; 1153.24]	J/mol×K	[273.00; 1000.00]	Joback Predicted correlation
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K
Coefficient A			8.92000e+00
Coefficient B			2.04768e+00
Coefficient C			-1.06316e-03
Coefficient D			1.59800e-07
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	491.95	J/mol×K	273.00	Calculated Property
Cp,gas	607.36	J/mol×K	353.78	Calculated Property
Cp,gas	711.10	J/mol×K	434.56	Calculated Property
Cp,gas	803.69	J/mol×K	515.33	Calculated Property
Cp,gas	885.62	J/mol×K	596.11	Calculated Property
Cp,gas	957.41	J/mol×K	676.89	Calculated Property
Cp,gas	1019.57	J/mol×K	757.67	Calculated Property
Cp,gas	1072.58	J/mol×K	838.44	Calculated Property
Cp,gas	1116.97	J/mol×K	919.22	Calculated Property
Cp,gas	1153.24	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.65]	kPa	[512.02; 762.10]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.26088e+01
Coefficient B			-4.47566e+03
Coefficient C			-1.48765e+02
Temperature range, min.			512.02
Temperature range, max.			762.10
Pvap	1.33	kPa	512.02	Calculated Property
Pvap	3.20	kPa	539.81	Calculated Property
Pvap	6.84	kPa	567.59	Calculated Property
Pvap	13.30	kPa	595.38	Calculated Property
Pvap	23.91	kPa	623.17	Calculated Property
Pvap	40.30	kPa	650.95	Calculated Property
Pvap	64.31	kPa	678.74	Calculated Property
Pvap	97.95	kPa	706.53	Calculated Property
Pvap	143.34	kPa	734.31	Calculated Property
Pvap	202.65	kPa	762.10	Calculated Property
Pvap	[9.39e-09; 1155.41]	kPa	[298.00; 806.00]	KDB Vapor Pressure Data
Equation			ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K
Coefficient A			1.60562e+02
Coefficient B			-2.04275e+04
Coefficient C			-1.94419e+01
Coefficient D			2.98773e-06
Coefficient E			0.00000e+00
Temperature range, min.			298.00
Temperature range, max.			806.00
Pvap	9.39e-09	kPa	298.00	Calculated Property
Pvap	1.98e-05	kPa	354.44	Calculated Property
Pvap	3.50e-03	kPa	410.89	Calculated Property
Pvap	0.13	kPa	467.33	Calculated Property
Pvap	1.92	kPa	523.78	Calculated Property
Pvap	14.08	kPa	580.22	Calculated Property
Pvap	64.50	kPa	636.67	Calculated Property
Pvap	211.11	kPa	693.11	Calculated Property
Pvap	540.72	kPa	749.56	Calculated Property
Pvap	1155.41	kPa	806.00	Calculated Property

Similar Compounds

Find more compounds similar to Bis(2-ethylhexyl) phthalate.

Mixtures

• n-Hexane + Bis(2-ethylhexyl) phthalate
• Toluene + Bis(2-ethylhexyl) phthalate
• Benzene, ethyl- + Bis(2-ethylhexyl) phthalate
• 1,2,4-Trimethylbenzene + Bis(2-ethylhexyl) phthalate

Sources

• KDB Vapor Pressure Data
• Cheméo Relay (1.0)
• 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

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.
Outlier This icon means that the value is more than 2 standard deviations away from the property mean.
These property values are available through the Cheméo API. A free account gives you an access key.