Chemical Properties of Hexanedioic acid, dimethyl ester (CAS 627-93-0)

InChI

InChI=1S/C8H14O4/c1-11-7(9)5-3-4-6-8(10)12-2/h3-6H2,1-2H3

InChI Key

UDSFAEKRVUSQDD-UHFFFAOYSA-N

Formula

C8H14O4

SMILES

COC(=O)CCCCC(=O)OC

Molecular Weight¹

174.19

CAS

627-93-0

Other Names

• 1,6-Dimethylhexanedioate
• 1,6-hexanedioic acid, dimethyl ester
• Dimethyl ester of hexanedioic acid
• Hexanedioic acid, methyl ester
• Methyl adipate
• adipic acid, dimethyl ester
• dimethyl 1,6-hexanedioate
• dimethyl adipate
• dimethyl hexanedioate

• ω : Acentric Factor.
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• Δ_cH°_solid : Standard solid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• η : Dynamic viscosity (Pa×s).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_liquid : Liquid phase 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).
• IE : Ionization energy (eV).
• 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).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• D^*_i : Self diffusion coefficient (m²/s).
• T_boil : Normal Boiling Point Temperature (K).
• T_boilr : Boiling point at reduced pressure (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. Pressure Dependent Properties
4. Datasets
5. Correlations
6. Similar Compounds
7. Mixtures
8. Sources

Physical Properties

Property	Value	Unit	Source
ω	0.6235		Relay (1.0) Calculated Property
ΔcH°liquid	-4286.20 ± 3.20	kJ/mol	NIST
ΔcH°solid	-4266.00	kJ/mol	NIST
ΔfH°gas	-817.90	kJ/mol	Relay (1.0) Calculated Property
ΔfH°liquid	-862.80 ± 3.20	kJ/mol	NIST
ΔfusH°	25.21	kJ/mol	Joback Calculated Property
ΔvapH°	[67.10; 73.40]	kJ/mol
ΔvapH°	67.10 ± 0.30	kJ/mol	NIST
ΔvapH°	69.00 ± 0.20	kJ/mol	NIST
ΔvapH°	73.40	kJ/mol	NIST
IE	9.82	eV	Relay (1.0) Calculated Property
log10WS	-1.32		Relay (1.0) Calculated Property
logPoct/wat	0.893		Crippen Calculated Property
McVol	138.460	ml/mol	McGowan Calculated Property
Pc	2500.00	kPa	Vapor Pressures, Enthalpies of Vaporization, and Critical Parameters of a Series of Linear Aliphatic Dimethyl Esters of Dicarboxylic Acids
Inp	[210.93; 1256.00]
Inp	1243.00		NIST
Inp	1242.00		NIST
Inp	1241.00		NIST
Inp	1207.00		NIST
Inp	1205.00		NIST
Inp	1204.00		NIST
Inp	1202.00		NIST
Inp	1234.00		NIST
Inp	1223.00		NIST
Inp	1208.20		NIST
Inp	1246.00		NIST
Inp	1206.00		NIST
Inp	1235.00		NIST
Inp	1256.00		NIST
Inp	1243.00		NIST
Inp	1205.00		NIST
Inp	1213.00		NIST
Inp	1246.70		NIST
Inp	1213.00		NIST
Inp	1212.00		NIST
Inp	1211.00		NIST
Inp	1215.00		NIST
Inp	1206.00		NIST
Inp	1206.00		NIST
Inp	1206.00		NIST
Inp	1212.00		NIST
Inp	1223.00		NIST
Inp	1213.00		NIST
Inp	Outlier 211.70		NIST
Inp	Outlier 210.93		NIST
Inp	1213.00		NIST
Inp	1243.00		NIST
Inp	1204.00		NIST
Inp	1206.00		NIST
I	[1777.00; 1819.00]
I	1777.00		NIST
I	1809.00		NIST
I	1817.00		NIST
I	1819.00		NIST
I	1804.00		NIST
I	1779.00		NIST
I	1777.00		NIST
I	1779.00		NIST
I	1817.00		NIST
Tboil	[498.20; 508.00]	K
Tboil	498.20	K	Liquid liquid equilibria of the ternary system water + acetic acid + dimethyl adipate
Tboil	508.00 ± 4.00	K	NIST
Tc	665.25	K	Relay (1.0) Calculated Property
Tfus	[283.50; 283.50]	K
Tfus	283.50 ± 0.60	K	NIST
Tfus	283.50 ± 1.00	K	NIST
Vc	0.534	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	[0.0009200; 0.0043900]	Pa×s	[283.15; 373.15]
η	0.0043900	Pa×s	283.15	Influence of the Molecular Structure on the Volumetric Properties and Viscosities of Dialkyl Adipates (Dimethyl, Diethyl, and Diisobutyl Adipates)
η	0.0038200	Pa×s	288.15	Influence of the Molecular Structure on the Volumetric Properties and Viscosities of Dialkyl Adipates (Dimethyl, Diethyl, and Diisobutyl Adipates)
η	0.0033600	Pa×s	293.15	Influence of the Molecular Structure on the Volumetric Properties and Viscosities of Dialkyl Adipates (Dimethyl, Diethyl, and Diisobutyl Adipates)
η	0.0029800	Pa×s	298.15	Influence of the Molecular Structure on the Volumetric Properties and Viscosities of Dialkyl Adipates (Dimethyl, Diethyl, and Diisobutyl Adipates)
η	0.0026700	Pa×s	303.15	Influence of the Molecular Structure on the Volumetric Properties and Viscosities of Dialkyl Adipates (Dimethyl, Diethyl, and Diisobutyl Adipates)
η	0.0024000	Pa×s	308.15	Influence of the Molecular Structure on the Volumetric Properties and Viscosities of Dialkyl Adipates (Dimethyl, Diethyl, and Diisobutyl Adipates)
η	0.0021800	Pa×s	313.15	Influence of the Molecular Structure on the Volumetric Properties and Viscosities of Dialkyl Adipates (Dimethyl, Diethyl, and Diisobutyl Adipates)
η	0.0019900	Pa×s	318.15	Influence of the Molecular Structure on the Volumetric Properties and Viscosities of Dialkyl Adipates (Dimethyl, Diethyl, and Diisobutyl Adipates)
η	0.0018200	Pa×s	323.15	Influence of the Molecular Structure on the Volumetric Properties and Viscosities of Dialkyl Adipates (Dimethyl, Diethyl, and Diisobutyl Adipates)
η	0.0016800	Pa×s	328.15	Influence of the Molecular Structure on the Volumetric Properties and Viscosities of Dialkyl Adipates (Dimethyl, Diethyl, and Diisobutyl Adipates)
η	0.0015500	Pa×s	333.15	Influence of the Molecular Structure on the Volumetric Properties and Viscosities of Dialkyl Adipates (Dimethyl, Diethyl, and Diisobutyl Adipates)
η	0.0014400	Pa×s	338.15	Influence of the Molecular Structure on the Volumetric Properties and Viscosities of Dialkyl Adipates (Dimethyl, Diethyl, and Diisobutyl Adipates)
η	0.0013400	Pa×s	343.15	Influence of the Molecular Structure on the Volumetric Properties and Viscosities of Dialkyl Adipates (Dimethyl, Diethyl, and Diisobutyl Adipates)
η	0.0012500	Pa×s	348.15	Influence of the Molecular Structure on the Volumetric Properties and Viscosities of Dialkyl Adipates (Dimethyl, Diethyl, and Diisobutyl Adipates)
η	0.0011700	Pa×s	353.15	Influence of the Molecular Structure on the Volumetric Properties and Viscosities of Dialkyl Adipates (Dimethyl, Diethyl, and Diisobutyl Adipates)
η	0.0011000	Pa×s	358.15	Influence of the Molecular Structure on the Volumetric Properties and Viscosities of Dialkyl Adipates (Dimethyl, Diethyl, and Diisobutyl Adipates)
η	0.0010300	Pa×s	363.15	Influence of the Molecular Structure on the Volumetric Properties and Viscosities of Dialkyl Adipates (Dimethyl, Diethyl, and Diisobutyl Adipates)
η	0.0009700	Pa×s	368.15	Influence of the Molecular Structure on the Volumetric Properties and Viscosities of Dialkyl Adipates (Dimethyl, Diethyl, and Diisobutyl Adipates)
η	0.0009200	Pa×s	373.15	Influence of the Molecular Structure on the Volumetric Properties and Viscosities of Dialkyl Adipates (Dimethyl, Diethyl, and Diisobutyl Adipates)
ΔvapH	[58.80; 74.60]	kJ/mol	[398.00; 441.00]
ΔvapH	74.60	kJ/mol	398.00	NIST
ΔvapH	58.80	kJ/mol	441.00	NIST
Pvap	[2.53e-03; 216.30]	kPa	[293.20; 531.44]
Pvap	2.53e-03	kPa	293.20	Thermodynamic Properties of Mixtures Containing Ionic Liquids. 7. Activity Coefficients of Aliphatic and Aromatic Esters and Benzylamine in 1-Methyl-3-ethylimidazolium Bis(trifluoromethylsulfonyl) Imide Using the Transpiration Method
Pvap	3.36e-03	kPa	296.20	Thermodynamic Properties of Mixtures Containing Ionic Liquids. 7. Activity Coefficients of Aliphatic and Aromatic Esters and Benzylamine in 1-Methyl-3-ethylimidazolium Bis(trifluoromethylsulfonyl) Imide Using the Transpiration Method
Pvap	4.43e-03	kPa	299.20	Thermodynamic Properties of Mixtures Containing Ionic Liquids. 7. Activity Coefficients of Aliphatic and Aromatic Esters and Benzylamine in 1-Methyl-3-ethylimidazolium Bis(trifluoromethylsulfonyl) Imide Using the Transpiration Method
Pvap	5.86e-03	kPa	302.20	Thermodynamic Properties of Mixtures Containing Ionic Liquids. 7. Activity Coefficients of Aliphatic and Aromatic Esters and Benzylamine in 1-Methyl-3-ethylimidazolium Bis(trifluoromethylsulfonyl) Imide Using the Transpiration Method
Pvap	7.40e-03	kPa	305.20	Thermodynamic Properties of Mixtures Containing Ionic Liquids. 7. Activity Coefficients of Aliphatic and Aromatic Esters and Benzylamine in 1-Methyl-3-ethylimidazolium Bis(trifluoromethylsulfonyl) Imide Using the Transpiration Method
Pvap	9.91e-03	kPa	308.20	Thermodynamic Properties of Mixtures Containing Ionic Liquids. 7. Activity Coefficients of Aliphatic and Aromatic Esters and Benzylamine in 1-Methyl-3-ethylimidazolium Bis(trifluoromethylsulfonyl) Imide Using the Transpiration Method
Pvap	0.01	kPa	310.20	Thermodynamic Properties of Mixtures Containing Ionic Liquids. 7. Activity Coefficients of Aliphatic and Aromatic Esters and Benzylamine in 1-Methyl-3-ethylimidazolium Bis(trifluoromethylsulfonyl) Imide Using the Transpiration Method
Pvap	0.01	kPa	313.30	Thermodynamic Properties of Mixtures Containing Ionic Liquids. 7. Activity Coefficients of Aliphatic and Aromatic Esters and Benzylamine in 1-Methyl-3-ethylimidazolium Bis(trifluoromethylsulfonyl) Imide Using the Transpiration Method
Pvap	0.02	kPa	316.20	Thermodynamic Properties of Mixtures Containing Ionic Liquids. 7. Activity Coefficients of Aliphatic and Aromatic Esters and Benzylamine in 1-Methyl-3-ethylimidazolium Bis(trifluoromethylsulfonyl) Imide Using the Transpiration Method
Pvap	0.02	kPa	319.30	Thermodynamic Properties of Mixtures Containing Ionic Liquids. 7. Activity Coefficients of Aliphatic and Aromatic Esters and Benzylamine in 1-Methyl-3-ethylimidazolium Bis(trifluoromethylsulfonyl) Imide Using the Transpiration Method
Pvap	0.03	kPa	322.20	Thermodynamic Properties of Mixtures Containing Ionic Liquids. 7. Activity Coefficients of Aliphatic and Aromatic Esters and Benzylamine in 1-Methyl-3-ethylimidazolium Bis(trifluoromethylsulfonyl) Imide Using the Transpiration Method
Pvap	0.04	kPa	325.30	Thermodynamic Properties of Mixtures Containing Ionic Liquids. 7. Activity Coefficients of Aliphatic and Aromatic Esters and Benzylamine in 1-Methyl-3-ethylimidazolium Bis(trifluoromethylsulfonyl) Imide Using the Transpiration Method
Pvap	0.05	kPa	328.20	Thermodynamic Properties of Mixtures Containing Ionic Liquids. 7. Activity Coefficients of Aliphatic and Aromatic Esters and Benzylamine in 1-Methyl-3-ethylimidazolium Bis(trifluoromethylsulfonyl) Imide Using the Transpiration Method
Pvap	0.06	kPa	331.20	Thermodynamic Properties of Mixtures Containing Ionic Liquids. 7. Activity Coefficients of Aliphatic and Aromatic Esters and Benzylamine in 1-Methyl-3-ethylimidazolium Bis(trifluoromethylsulfonyl) Imide Using the Transpiration Method
Pvap	0.07	kPa	334.20	Thermodynamic Properties of Mixtures Containing Ionic Liquids. 7. Activity Coefficients of Aliphatic and Aromatic Esters and Benzylamine in 1-Methyl-3-ethylimidazolium Bis(trifluoromethylsulfonyl) Imide Using the Transpiration Method
Pvap	0.51	kPa	353.15	Vapor-Liquid Equilibrium of Mixtures Containing Adipic Acid, Glutaric Acid, Dimethyl Adipate, Dimethyl Glutarate, Methanol, and Water
Pvap	1.26	kPa	373.15	Vapor-Liquid Equilibrium of Mixtures Containing Adipic Acid, Glutaric Acid, Dimethyl Adipate, Dimethyl Glutarate, Methanol, and Water
Pvap	1.92	kPa	383.15	Vapor-Liquid Equilibrium of Mixtures Containing Adipic Acid, Glutaric Acid, Dimethyl Adipate, Dimethyl Glutarate, Methanol, and Water
Pvap	2.00	kPa	390.98	Isobaric vapor-liquid equilibrium of three binary systems containing dimethyl succinate, dimethyl glutarate and dimethyl adipate at 2, 5.2 and 8.3 kPa
Pvap	4.33	kPa	403.15	Vapor-Liquid Equilibrium of Mixtures Containing Adipic Acid, Glutaric Acid, Dimethyl Adipate, Dimethyl Glutarate, Methanol, and Water
Pvap	5.20	kPa	410.82	Isobaric vapor-liquid equilibrium of three binary systems containing dimethyl succinate, dimethyl glutarate and dimethyl adipate at 2, 5.2 and 8.3 kPa
Pvap	5.93	kPa	413.15	Vapor-Liquid Equilibrium of Mixtures Containing Adipic Acid, Glutaric Acid, Dimethyl Adipate, Dimethyl Glutarate, Methanol, and Water
Pvap	8.30	kPa	422.47	Isobaric vapor-liquid equilibrium of three binary systems containing dimethyl succinate, dimethyl glutarate and dimethyl adipate at 2, 5.2 and 8.3 kPa
Pvap	8.37	kPa	423.15	Vapor-Liquid Equilibrium of Mixtures Containing Adipic Acid, Glutaric Acid, Dimethyl Adipate, Dimethyl Glutarate, Methanol, and Water
Pvap	7.79	kPa	424.91	Isobaric Vapor-Liquid Equilibrium for the Binary System of Dimethyl Adipate and 1,6-Hexanediol at 10, 20, and 99 kPa
Pvap	10.00	kPa	431.20	Isobaric Vapor-Liquid Equilibrium for the Binary System of Dimethyl Adipate and 1,6-Hexanediol at 10, 20, and 99 kPa
Pvap	12.30	kPa	433.15	Vapor-Liquid Equilibrium of Mixtures Containing Adipic Acid, Glutaric Acid, Dimethyl Adipate, Dimethyl Glutarate, Methanol, and Water
Pvap	14.56	kPa	441.21	Isobaric Vapor-Liquid Equilibrium for the Binary System of Dimethyl Adipate and 1,6-Hexanediol at 10, 20, and 99 kPa
Pvap	16.66	kPa	443.15	Vapor-Liquid Equilibrium of Mixtures Containing Adipic Acid, Glutaric Acid, Dimethyl Adipate, Dimethyl Glutarate, Methanol, and Water
Pvap	20.00	kPa	450.08	Isobaric Vapor-Liquid Equilibrium for the Binary System of Dimethyl Adipate and 1,6-Hexanediol at 10, 20, and 99 kPa
Pvap	28.55	kPa	460.47	Isobaric Vapor-Liquid Equilibrium for the Binary System of Dimethyl Adipate and 1,6-Hexanediol at 10, 20, and 99 kPa
Pvap	44.63	kPa	474.33	Isobaric Vapor-Liquid Equilibrium for the Binary System of Dimethyl Adipate and 1,6-Hexanediol at 10, 20, and 99 kPa
Pvap	54.37	kPa	480.72	Isobaric Vapor-Liquid Equilibrium for the Binary System of Dimethyl Adipate and 1,6-Hexanediol at 10, 20, and 99 kPa
Pvap	68.77	kPa	488.62	Isobaric Vapor-Liquid Equilibrium for the Binary System of Dimethyl Adipate and 1,6-Hexanediol at 10, 20, and 99 kPa
Pvap	85.45	kPa	496.14	Isobaric Vapor-Liquid Equilibrium for the Binary System of Dimethyl Adipate and 1,6-Hexanediol at 10, 20, and 99 kPa
Pvap	99.00	kPa	501.00	Isobaric Vapor-Liquid Equilibrium for the Binary System of Dimethyl Adipate and 1,6-Hexanediol at 10, 20, and 99 kPa
Pvap	108.77	kPa	504.86	Isobaric Vapor-Liquid Equilibrium for the Binary System of Dimethyl Adipate and 1,6-Hexanediol at 10, 20, and 99 kPa
Pvap	131.95	kPa	512.00	Isobaric Vapor-Liquid Equilibrium for the Binary System of Dimethyl Adipate and 1,6-Hexanediol at 10, 20, and 99 kPa
Pvap	157.68	kPa	518.78	Isobaric Vapor-Liquid Equilibrium for the Binary System of Dimethyl Adipate and 1,6-Hexanediol at 10, 20, and 99 kPa
Pvap	179.21	kPa	523.92	Isobaric Vapor-Liquid Equilibrium for the Binary System of Dimethyl Adipate and 1,6-Hexanediol at 10, 20, and 99 kPa
Pvap	216.30	kPa	531.44	Isobaric Vapor-Liquid Equilibrium for the Binary System of Dimethyl Adipate and 1,6-Hexanediol at 10, 20, and 99 kPa
n0	[1.41614; 1.43050]		[288.15; 323.15]
n0	1.43050		288.15	Experimental Determination and Modeling of Densities, Refractive Indices of the Binary Mixtures of Dimethylphthalate (or Dimethyladipate) + 1-Butanol, or + 2-Butanol, or + 2-Butanone at T = (288.15 to 323.15) K
n0	1.42825		293.15	Phase equilibria of (water + levulinic acid + dibasic esters) ternary systems
n0	1.42825		293.15	(Liquid + liquid) equilibria of (water + butyric acid + dibasic esters) ternary systems
n0	1.42825		293.15	(Liquid + liquid) equilibria of (water + propionic acid + dibasic esters) ternary systems
n0	1.42842		293.15	Experimental Determination and Modeling of Densities, Refractive Indices of the Binary Mixtures of Dimethylphthalate (or Dimethyladipate) + 1-Butanol, or + 2-Butanol, or + 2-Butanone at T = (288.15 to 323.15) K
n0	1.42825		293.20	Liquid-Liquid Equilibria for Ternary Systems of Water + Formic Acid + Dibasic Esters
n0	1.42636		298.15	Experimental Determination and Modeling of Densities, Refractive Indices of the Binary Mixtures of Dimethylphthalate (or Dimethyladipate) + 1-Butanol, or + 2-Butanol, or + 2-Butanone at T = (288.15 to 323.15) K
n0	1.42429		303.15	Experimental Determination and Modeling of Densities, Refractive Indices of the Binary Mixtures of Dimethylphthalate (or Dimethyladipate) + 1-Butanol, or + 2-Butanol, or + 2-Butanone at T = (288.15 to 323.15) K
n0	1.42222		308.15	Experimental Determination and Modeling of Densities, Refractive Indices of the Binary Mixtures of Dimethylphthalate (or Dimethyladipate) + 1-Butanol, or + 2-Butanol, or + 2-Butanone at T = (288.15 to 323.15) K
n0	1.42017		313.15	Experimental Determination and Modeling of Densities, Refractive Indices of the Binary Mixtures of Dimethylphthalate (or Dimethyladipate) + 1-Butanol, or + 2-Butanol, or + 2-Butanone at T = (288.15 to 323.15) K
n0	1.41819		318.15	Experimental Determination and Modeling of Densities, Refractive Indices of the Binary Mixtures of Dimethylphthalate (or Dimethyladipate) + 1-Butanol, or + 2-Butanol, or + 2-Butanone at T = (288.15 to 323.15) K
n0	1.41614		323.15	Experimental Determination and Modeling of Densities, Refractive Indices of the Binary Mixtures of Dimethylphthalate (or Dimethyladipate) + 1-Butanol, or + 2-Butanol, or + 2-Butanone at T = (288.15 to 323.15) K
ρl	[1032.62; 1066.79]	kg/m3	[288.15; 323.15]
ρl	1066.79	kg/m3	288.15	Experimental Investigation of Interactions and Thermodynamic Properties of Poly(ethylene glycol) 200/400 + Dimethyl Adipate/Dimethyl Phthalate Binary Mixtures
ρl	1061.92	kg/m3	293.15	Experimental Investigation of Interactions and Thermodynamic Properties of Poly(ethylene glycol) 200/400 + Dimethyl Adipate/Dimethyl Phthalate Binary Mixtures
ρl	1061.93	kg/m3	293.15	Thermodynamic and Spectroscopic Study of the Ternary System Dimethyladipate + Tetrahydrofuran +1-Butanol at T = (288.15 to 323.15) K
ρl	1061.93	kg/m3	293.15	Densities, Viscosities and Refractive Indices of the Ternary Mixture Dimethyladipate + 2-Butanone + 1-Butanol at T = (288.15 to 323.15) K
ρl	1057.05	kg/m3	298.15	Experimental Investigation of Interactions and Thermodynamic Properties of Poly(ethylene glycol) 200/400 + Dimethyl Adipate/Dimethyl Phthalate Binary Mixtures
ρl	1052.18	kg/m3	303.15	Experimental Investigation of Interactions and Thermodynamic Properties of Poly(ethylene glycol) 200/400 + Dimethyl Adipate/Dimethyl Phthalate Binary Mixtures
ρl	1047.30	kg/m3	308.15	Experimental Investigation of Interactions and Thermodynamic Properties of Poly(ethylene glycol) 200/400 + Dimethyl Adipate/Dimethyl Phthalate Binary Mixtures
ρl	1042.41	kg/m3	313.15	Experimental Investigation of Interactions and Thermodynamic Properties of Poly(ethylene glycol) 200/400 + Dimethyl Adipate/Dimethyl Phthalate Binary Mixtures
ρl	1037.52	kg/m3	318.15	Experimental Investigation of Interactions and Thermodynamic Properties of Poly(ethylene glycol) 200/400 + Dimethyl Adipate/Dimethyl Phthalate Binary Mixtures
ρl	1032.62	kg/m3	323.15	Experimental Investigation of Interactions and Thermodynamic Properties of Poly(ethylene glycol) 200/400 + Dimethyl Adipate/Dimethyl Phthalate Binary Mixtures
D*i	[0.00; 0.00]	m2/s	[293.43; 338.47]
D*i	0.00	m2/s	293.43	Self-diffusivity measurements of dimethyl, diethyl, dipropyl, dibutyl, Bis(2-ethylhexyl) adipates from (293 - 339) K by a PGSE-NMR spin-echo technique
D*i	0.00	m2/s	302.44	Self-diffusivity measurements of dimethyl, diethyl, dipropyl, dibutyl, Bis(2-ethylhexyl) adipates from (293 - 339) K by a PGSE-NMR spin-echo technique
D*i	0.00	m2/s	311.45	Self-diffusivity measurements of dimethyl, diethyl, dipropyl, dibutyl, Bis(2-ethylhexyl) adipates from (293 - 339) K by a PGSE-NMR spin-echo technique
D*i	0.00	m2/s	320.46	Self-diffusivity measurements of dimethyl, diethyl, dipropyl, dibutyl, Bis(2-ethylhexyl) adipates from (293 - 339) K by a PGSE-NMR spin-echo technique
D*i	0.00	m2/s	329.45	Self-diffusivity measurements of dimethyl, diethyl, dipropyl, dibutyl, Bis(2-ethylhexyl) adipates from (293 - 339) K by a PGSE-NMR spin-echo technique
D*i	0.00	m2/s	338.47	Self-diffusivity measurements of dimethyl, diethyl, dipropyl, dibutyl, Bis(2-ethylhexyl) adipates from (293 - 339) K by a PGSE-NMR spin-echo technique

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboilr	382.70	K	1.90	NIST

Datasets

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

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
293.17	100.00	0.0033
293.17	1000.00	0.0033
293.15	5000.00	0.0035
293.15	10000.00	0.0036
293.15	15000.00	0.0038
293.15	20000.00	0.0040
293.15	30000.00	0.0043
293.15	40000.00	0.0047
303.17	100.00	0.0026
303.17	1000.00	0.0026
303.15	5000.00	0.0027
303.15	10000.00	0.0029
303.16	15000.00	0.0030
303.16	20000.00	0.0031
303.16	30000.00	0.0034
303.16	40000.00	0.0037
313.15	100.00	0.0021
313.14	1000.00	0.0022
313.15	5000.00	0.0022
313.15	10000.00	0.0023
313.14	15000.00	0.0024
313.14	20000.00	0.0025
313.14	30000.00	0.0027
313.15	40000.00	0.0030
323.15	100.00	0.0018
323.15	1000.00	0.0018
323.15	5000.00	0.0018
323.15	10000.00	0.0019
323.15	15000.00	0.0020
323.15	20000.00	0.0021
323.15	30000.00	0.0023
323.14	40000.00	0.0024
333.15	100.00	0.0015
333.15	1000.00	0.0015
333.15	5000.00	0.0016
333.15	10000.00	0.0016
333.15	15000.00	0.0017
333.15	20000.00	0.0018
333.15	30000.00	0.0019
333.14	40000.00	0.0020
343.15	100.00	0.0013
343.15	1000.00	0.0013
343.15	5000.00	0.0013
343.15	10000.00	0.0014
343.15	15000.00	0.0015
343.15	20000.00	0.0015
343.15	30000.00	0.0016
343.15	40000.00	0.0018
353.15	100.00	0.0011
353.16	1000.00	0.0011
353.15	5000.00	0.0012
353.15	10000.00	0.0012
353.15	15000.00	0.0013
353.15	20000.00	0.0013
353.15	30000.00	0.0014
353.15	40000.00	0.0015
363.15	100.00	0.0010
363.15	1000.00	0.0010
363.15	5000.00	0.0010
363.15	10000.00	0.0011
363.13	15000.00	0.0011
363.13	20000.00	0.0012
363.15	30000.00	0.0012
363.15	40000.00	0.0013
Reference

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.15	100.00	1061.2
293.15	4990.00	1064.2
293.15	10010.00	1067.3
293.15	20020.00	1073.2
293.15	25000.00	1076.0
293.15	14980.00	1070.3
293.15	7490.00	1065.8
293.15	5000.00	1064.3
293.15	2510.00	1062.8
323.15	100.00	1031.9
323.15	4990.00	1035.5
323.15	10060.00	1039.1
323.15	20020.00	1045.8
323.15	24990.00	1049.0
323.15	15010.00	1042.5
323.15	7490.00	1037.3
323.15	5000.00	1035.5
323.15	2540.00	1033.7
358.15	100.00	997.6
358.15	4980.00	1001.9
358.15	9980.00	1006.1
358.15	20030.00	1014.2
358.15	25000.00	1018.0
358.15	15030.00	1010.3
358.15	7500.00	1004.1
358.15	5020.00	1002.0
358.15	2500.00	999.8
303.15	100.00	1051.5
303.15	5010.00	1054.7
303.15	9990.00	1057.9
303.15	20000.00	1064.0
303.15	25000.00	1067.0
303.15	15010.00	1061.0
303.15	7510.00	1056.3
303.15	5010.00	1054.7
303.15	2510.00	1053.1
333.15	100.00	1022.1
333.15	5010.00	1026.0
333.15	10020.00	1029.7
333.15	20030.00	1036.8
333.15	24920.00	1040.1
333.15	15000.00	1033.2
333.15	7490.00	1027.8
333.15	5040.00	1026.0
333.15	2520.00	1024.1
293.15	100.00	1061.2
293.15	5020.00	1064.3
293.15	10020.00	1067.3
293.15	20240.00	1073.3
293.15	25010.00	1076.0
293.15	15030.00	1070.3
293.15	7570.00	1065.9
293.15	5030.00	1064.3
293.15	2540.00	1062.8
313.15	100.00	1041.8
313.15	5020.00	1045.2
313.15	10010.00	1048.5
313.15	20020.00	1054.9
313.15	25000.00	1058.0
313.15	15010.00	1051.7
313.15	7520.00	1046.8
313.15	5020.00	1045.1
313.15	2520.00	1043.5
343.15	100.00	1012.4
343.15	5010.00	1016.3
343.15	9990.00	1020.2
343.15	20000.00	1027.7
343.15	24990.00	1031.2
343.15	15010.00	1024.0
343.15	7530.00	1018.3
343.15	5000.00	1016.3
343.15	2500.00	1014.3
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[207.87; 448.27]	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			4.64340e+01
Coefficient B			6.54240e-01
Coefficient C			-2.22200e-04
Coefficient D			-3.02000e-08
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	207.87	J/mol×K	273.00	Calculated Property
Cp,gas	248.74	J/mol×K	353.78	Calculated Property
Cp,gas	286.30	J/mol×K	434.56	Calculated Property
Cp,gas	320.44	J/mol×K	515.33	Calculated Property
Cp,gas	351.08	J/mol×K	596.11	Calculated Property
Cp,gas	378.11	J/mol×K	676.89	Calculated Property
Cp,gas	401.44	J/mol×K	757.67	Calculated Property
Cp,gas	420.97	J/mol×K	838.44	Calculated Property
Cp,gas	436.62	J/mol×K	919.22	Calculated Property
Cp,gas	448.27	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.63]	kPa	[378.68; 537.32]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.73676e+01
Coefficient B			-6.50271e+03
Coefficient C			2.04500e+00
Temperature range, min.			378.68
Temperature range, max.			537.32
Pvap	1.33	kPa	378.68	Calculated Property
Pvap	2.84	kPa	396.31	Calculated Property
Pvap	5.67	kPa	413.93	Calculated Property
Pvap	10.71	kPa	431.56	Calculated Property
Pvap	19.23	kPa	449.19	Calculated Property
Pvap	33.06	kPa	466.81	Calculated Property
Pvap	54.65	kPa	484.44	Calculated Property
Pvap	87.21	kPa	502.07	Calculated Property
Pvap	134.84	kPa	519.69	Calculated Property
Pvap	202.63	kPa	537.32	Calculated Property

Similar Compounds

Find more compounds similar to Hexanedioic acid, dimethyl ester.

Mixtures

• 1-Butanol + Hexanedioic acid, dimethyl ester
• 2-Butanone + Hexanedioic acid, dimethyl ester
• Pentanoic acid, 4-oxo- + Hexanedioic acid, dimethyl ester + Water
• Pentanedioic acid, dimethyl ester + Hexanedioic acid, dimethyl ester
• Hexanedioic acid, dimethyl ester + Butanedioic acid, dimethyl ester
• Hexanedioic acid, dimethyl ester + Propanoic acid + Water
• Hexanedioic acid, dimethyl ester + Water
• Hexanedioic acid, dimethyl ester + Methyl Alcohol + Water
• Hexanedioic acid, dimethyl ester + Hexanedioic acid, monomethyl ester + Water
• Butanoic acid + Hexanedioic acid, dimethyl ester + Water
• Acetic acid + Hexanedioic acid, dimethyl ester + Water
• Hexanedioic acid, dimethyl ester + Methyl Alcohol
• Formic acid + Hexanedioic acid, dimethyl ester + Water
• 1-Butanol + Hexanedioic acid, dimethyl ester + Tetrahydrofuran
• Hexanedioic acid + Hexanedioic acid, dimethyl ester + Methyl Alcohol
• Hexanedioic acid, dimethyl ester + Methyl Alcohol + Pentanedioic acid
• Butanedioic acid + Hexanedioic acid, dimethyl ester + Methyl Alcohol
• Hexanedioic acid + Hexanedioic acid, dimethyl ester
• Hexanedioic acid, dimethyl ester + Pentanedioic acid
• Butanedioic acid + Hexanedioic acid, dimethyl ester

Find more mixtures with Hexanedioic acid, dimethyl ester.

Sources

• Cheméo Relay (1.0)
• Crippen Method
• Crippen Method
• Viscosity Measurements of Dialkyl Adipates in the Temperature Range of (283 to 363) K and up to 40 MPa
• Liquid liquid equilibria of the ternary system water + acetic acid + dimethyl adipate
• Liquid liquid equilibria of aqueous mixtures containing selected dibasic esters and/or methanol
• Phase equilibria of (water + levulinic acid + dibasic esters) ternary systems
• Viscosity and density measurements of compressed liquid dimethyl adipate using oscillating body techniques
• (Liquid + liquid) equilibria of the (water + carboxylic acid + dibasic esters mixture (DBE-2)) ternary systems
• Self-diffusivity measurements of dimethyl, diethyl, dipropyl, dibutyl, Bis(2-ethylhexyl) adipates from (293 - 339) K by a PGSE-NMR spin-echo technique
• (Liquid + liquid) equilibria of (water + butyric acid + dibasic esters) ternary systems
• (Liquid + liquid) equilibria of (water + propionic acid + dibasic esters) ternary systems
• Isobaric vapor-liquid equilibrium of three binary systems containing dimethyl succinate, dimethyl glutarate and dimethyl adipate at 2, 5.2 and 8.3 kPa
• Experimental Determination and Modeling of Densities, Refractive Indices of the Binary Mixtures of Dimethylphthalate (or Dimethyladipate) + 1-Butanol, or + 2-Butanol, or + 2-Butanone at T = (288.15 to 323.15) K
• Experimental Investigation of Interactions and Thermodynamic Properties of Poly(ethylene glycol) 200/400 + Dimethyl Adipate/Dimethyl Phthalate Binary Mixtures
• Thermophysical Properties and Solubility of Different Sugar-Derived Molecules in Deep Eutectic Solvents
• Measurement and Correlation for Solubilities of Adipic Acid, Glutaric Acid, and Succinic Acid in Dimethyl Adipate + Methanol Mixtures
• Isobaric Vapor-Liquid Equilibrium for the Binary System of Dimethyl Adipate and 1,6-Hexanediol at 10, 20, and 99 kPa
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 7. Activity Coefficients of Aliphatic and Aromatic Esters and Benzylamine in 1-Methyl-3-ethylimidazolium Bis(trifluoromethylsulfonyl) Imide Using the Transpiration Method
• Vapor Pressures, Enthalpies of Vaporization, and Critical Parameters of a Series of Linear Aliphatic Dimethyl Esters of Dicarboxylic Acids
• Influence of the Molecular Structure on the Volumetric Properties and Viscosities of Dialkyl Adipates (Dimethyl, Diethyl, and Diisobutyl Adipates)
• Thermodynamic and Spectroscopic Study of the Ternary System Dimethyladipate + Tetrahydrofuran +1-Butanol at T = (288.15 to 323.15) K
• Densities, Viscosities and Refractive Indices of the Ternary Mixture Dimethyladipate + 2-Butanone + 1-Butanol at T = (288.15 to 323.15) K
• Vapor-Liquid Equilibrium of Mixtures Containing Adipic Acid, Glutaric Acid, Dimethyl Adipate, Dimethyl Glutarate, Methanol, and Water
• Liquid-Liquid Equilibria for Ternary Systems of Water + Formic Acid + Dibasic Esters
• Joback Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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