Chemical Properties of Ethane, 1,2-dimethoxy- (CAS 110-71-4)

InChI

InChI=1S/C4H10O2/c1-5-3-4-6-2/h3-4H2,1-2H3

InChI Key

XTHFKEDIFFGKHM-UHFFFAOYSA-N

Formula

C4H10O2

SMILES

COCCOC

Molecular Weight¹

90.12

CAS

110-71-4

Other Names

• 1,2-Ethanediol dimethyl ether
• 1,2-dimethoxyethane
• 1,2-ethanediol, dimethyl ether
• 2,5-dioxahexane
• Ansul ether 121
• CH3OCH2CH2OCH3
• DME
• DME (glycol ether)
• Dimethoxyethane
• Dimethyl cellosolve
• Egdme
• Ethylene dimethyl ether
• Glycol dimethyl ether
• Glyme
• Hisolve MMM
• Monoethylene glycol dimethyl ether
• NSC 60542
• UN 2252
• dimethylglycol
• ethylene glycol dimethyl ether
• monoglyme
• «alpha»,«beta»-Dimethoxyethane

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• BasG : Gas basicity (kJ/mol).
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• ε_r : Dielectric Constant (Relative permittivity).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• 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_c : Critical density (kg/m³).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• c_sound,fluid : Speed of sound in fluid (m/s).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• λ : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• V_c : Critical Volume (m³/kmol).
• Z_c : Critical Compressibility.
• 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	0.3580		KDB
PAff	[846.00; 858.00]	kJ/mol
PAff	858.00	kJ/mol	NIST
PAff	846.00 ± 2.00	kJ/mol	NIST
BasG	820.20	kJ/mol	NIST
ΔcH°liquid	-2623.60 ± 1.50	kJ/mol	NIST
μ	0.00	debye	KDB
ΔfG°	-227.20	kJ/mol	Joback Calculated Property
ΔfH°gas	[-390.00; -340.50]	kJ/mol
ΔfH°gas	-342.80 ± 0.70	kJ/mol	NIST
ΔfH°gas	-390.00 ± 2.00	kJ/mol	NIST
ΔfH°gas	-340.50 ± 0.63	kJ/mol	NIST
ΔfH°liquid	[-420.00; -376.60]	kJ/mol
ΔfH°liquid	-379.56 ± 0.64	kJ/mol	NIST
ΔfH°liquid	-420.00 ± 2.00	kJ/mol	NIST
ΔfH°liquid	-376.60 ± 0.20	kJ/mol	NIST
ΔfusH°	8.49	kJ/mol	Joback Calculated Property
ΔvapH°	[30.00; 36.80]	kJ/mol
ΔvapH°	36.47	kJ/mol	NIST
ΔvapH°	36.76 ± 0.23	kJ/mol	NIST
ΔvapH°	36.80	kJ/mol	NIST
ΔvapH°	36.80 ± 0.20	kJ/mol	NIST
ΔvapH°	Outlier 30.00	kJ/mol	NIST
ΔvapH°	36.39 ± 0.02	kJ/mol	NIST
ΔvapH°	36.20 ± 0.42	kJ/mol	NIST
ΔvapH°	36.10	kJ/mol	NIST
IE	[9.20; 9.90]	eV
IE	9.30	eV	NIST
IE	9.30	eV	NIST
IE	9.20	eV	NIST
IE	9.90	eV	NIST
IE	9.78	eV	NIST
log10WS	0.31		Relay (1.0) Calculated Property
logPoct/wat	0.279		Crippen Calculated Property
McVol	78.960	ml/mol	McGowan Calculated Property
Pc	[3860.00; 3960.00]	kPa
Pc	3870.00	kPa	KDB
Pc	3960.00 ± 250.00	kPa	NIST
Pc	3860.00 ± 20.00	kPa	NIST
Pc	3870.00 ± 27.57	kPa	NIST
ρc	292.89 ± 11.72	kg/m3	NIST
Inp	[607.00; 646.00]
Inp	646.00		NIST
Inp	635.00		NIST
Inp	607.00		NIST
Inp	608.00		NIST
Inp	645.00		NIST
Inp	646.00		NIST
Inp	641.00		NIST
Inp	641.00		NIST
Inp	609.50		NIST
Inp	614.50		NIST
Inp	646.00		NIST
I	[918.00; 935.00]
I	918.00		NIST
I	935.00		NIST
I	935.00		NIST
I	935.00		NIST
Tboil	[356.70; 358.35]	K
Tboil	357.75	K	Isobaric Vapor-Liquid Equilibrium Data for Two Binary Systems n-Hexane + 1,2-Dimethoxyethane and Methylcyclopentane + 1,2-Dimethoxyethane at 101.3 kPa
Tboil	358.00	K	KDB
Tboil	358.10 ± 0.40	K	NIST
Tboil	358.22 ± 0.40	K	NIST
Tboil	358.20	K	NIST
Tboil	356.70	K	NIST
Tboil	358.00	K	NIST
Tboil	358.35	K	NIST
Tboil	358.31 ± 0.10	K	NIST
Tboil	357.65 ± 0.50	K	NIST
Tboil	358.35 ± 0.70	K	NIST
Tboil	357.00 ± 2.00	K	NIST
Tboil	356.90 ± 1.00	K	NIST
Tc	[535.32; 539.20]	K
Tc	535.32	K	DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development
Tc	536.00	K	KDB
Tc	537.00 ± 2.00	K	NIST
Tc	539.20 ± 0.50	K	NIST
Tc	536.00 ± 2.00	K	NIST
Tfus	[203.41; 215.00]	K
Tfus	203.41	K	Efficient determination of crystallisation and melting points at low cooling and heating rates with novel computer controlled equipment
Tfus	215.00	K	KDB
Tfus	203.94 ± 0.10	K	NIST
Tfus	204.15	K	NIST
Vc	[0.271; 0.271]	m3/kmol
Vc	0.271	m3/kmol	KDB
Vc	0.271 ± 0.005	m3/kmol	NIST
Zc	0.2353310		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[137.10; 177.10]	J/mol×K	[335.76; 500.99]
Cp,gas	137.10	J/mol×K	335.76	Joback Calculated Property
Cp,gas	143.99	J/mol×K	363.30	Joback Calculated Property
Cp,gas	150.81	J/mol×K	390.84	Joback Calculated Property
Cp,gas	157.53	J/mol×K	418.37	Joback Calculated Property
Cp,gas	164.16	J/mol×K	445.91	Joback Calculated Property
Cp,gas	170.69	J/mol×K	473.45	Joback Calculated Property
Cp,gas	177.10	J/mol×K	500.99	Joback Calculated Property
Cp,liquid	[188.70; 196.90]	J/mol×K	[288.15; 323.15]
Cp,liquid	188.70	J/mol×K	288.15	Thermophysical properties of dimethyl sulfoxide + cyclic and linear ethers at 308.15K Application of an extended cell model
Cp,liquid	189.00	J/mol×K	293.15	Thermophysical properties of dimethyl sulfoxide + cyclic and linear ethers at 308.15K Application of an extended cell model
Cp,liquid	191.00	J/mol×K	298.15	Thermophysical properties of dimethyl sulfoxide + cyclic and linear ethers at 308.15K Application of an extended cell model
Cp,liquid	191.14	J/mol×K	298.15	NIST
Cp,liquid	193.30	J/mol×K	298.15	NIST
Cp,liquid	192.20	J/mol×K	303.15	Thermophysical properties of dimethyl sulfoxide + cyclic and linear ethers at 308.15K Application of an extended cell model
Cp,liquid	193.40	J/mol×K	308.15	Thermophysical properties of dimethyl sulfoxide + cyclic and linear ethers at 308.15K Application of an extended cell model
Cp,liquid	194.50	J/mol×K	313.15	Thermophysical properties of dimethyl sulfoxide + cyclic and linear ethers at 308.15K Application of an extended cell model
Cp,liquid	195.80	J/mol×K	318.15	Thermophysical properties of dimethyl sulfoxide + cyclic and linear ethers at 308.15K Application of an extended cell model
Cp,liquid	196.90	J/mol×K	323.15	Thermophysical properties of dimethyl sulfoxide + cyclic and linear ethers at 308.15K Application of an extended cell model
η	[0.0003300; 0.0004090]	Pa×s	[298.15; 318.15]
η	0.0004090	Pa×s	298.15	Viscosity, Density, and Speed of Sound for the Binary Mixtures of Formamide with 2-Methoxyethanol, Acetophenone, Acetonitrile, 1,2-Dimethoxyethane, and Dimethylsulfoxide at Different Temperatures
η	0.0003660	Pa×s	308.15	Viscosity, Density, and Speed of Sound for the Binary Mixtures of Formamide with 2-Methoxyethanol, Acetophenone, Acetonitrile, 1,2-Dimethoxyethane, and Dimethylsulfoxide at Different Temperatures
η	0.0003300	Pa×s	318.15	Viscosity, Density, and Speed of Sound for the Binary Mixtures of Formamide with 2-Methoxyethanol, Acetophenone, Acetonitrile, 1,2-Dimethoxyethane, and Dimethylsulfoxide at Different Temperatures
εr	[6.75; 7.41]		[288.15; 308.15]
εr	7.41		288.15	Permittivity and density of the systems (monoglyme, diglyme, triglyme, or tetraglyme + n-heptane) at several temperatures
εr	7.07		298.15	Permittivity and density of the systems (monoglyme, diglyme, triglyme, or tetraglyme + n-heptane) at several temperatures
εr	6.75		308.15	Permittivity and density of the systems (monoglyme, diglyme, triglyme, or tetraglyme + n-heptane) at several temperatures
ΔvapH	[32.42; 39.40]	kJ/mol	[268.00; 358.00]
ΔvapH	39.40	kJ/mol	268.00	NIST
ΔvapH	33.90	kJ/mol	295.50	NIST
ΔvapH	39.10	kJ/mol	300.50	NIST
ΔvapH	34.50	kJ/mol	331.00	NIST
ΔvapH	32.42	kJ/mol	358.00	NIST
Pvap	101.30	kPa	357.75	Isobaric Vapor-Liquid Equilibrium Data for Two Binary Systems n-Hexane + 1,2-Dimethoxyethane and Methylcyclopentane + 1,2-Dimethoxyethane at 101.3 kPa
n0	[1.36720; 1.38240]		[288.15; 318.15]
n0	1.38229		288.15	Study of static permittivity and density of the systems {(n-nonane + monoglyme or diglyme)} at various temperatures
n0	1.38240		288.15	Liquid Densities and Refractive Indices of Binary Mixtures for the Dimethyl Ether of a Glycol + Ethanol from T=288.15 K to 318.15 K
n0	1.37810		298.15	Bubble temperature measurements on the binary mixtures formed by decane with a variety of compounds at 95.8 kPa
n0	1.37900		298.15	Non-ideal behaviour of a room temperature ionic liquid in an alkoxyethanol or poly ethers at T = (298.15 to 318.15) K
n0	1.37718		298.15	Study of static permittivity and density of the systems {(n-nonane + monoglyme or diglyme)} at various temperatures
n0	1.37810		298.15	Bubble Temperature Measurements on Binary Mixtures Formed by Cyclohexane at 94.7 kPa
n0	1.37830		298.15	Solubility of -Carotene in Binary Solvents Formed by Some Hydrocarbons with Dibutyl Ether and 1,2-Dimethoxyethane
n0	1.37720		298.15	Liquid Densities and Refractive Indices of Binary Mixtures for the Dimethyl Ether of a Glycol + Ethanol from T=288.15 K to 318.15 K
n0	1.37197		308.15	Study of static permittivity and density of the systems {(n-nonane + monoglyme or diglyme)} at various temperatures
n0	1.37220		308.15	Liquid Densities and Refractive Indices of Binary Mixtures for the Dimethyl Ether of a Glycol + Ethanol from T=288.15 K to 318.15 K
n0	1.36720		318.15	Liquid Densities and Refractive Indices of Binary Mixtures for the Dimethyl Ether of a Glycol + Ethanol from T=288.15 K to 318.15 K
ρl	[821.86; 877.72]	kg/m3	[283.15; 333.15]
ρl	877.72	kg/m3	283.15	Densities and Viscosities of Three Binary Monoglyme + 1-Alcohol Systems from (283.15 to 313.15) K
ρl	877.64	kg/m3	283.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	876.56	kg/m3	284.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	875.48	kg/m3	285.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	874.40	kg/m3	286.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	873.31	kg/m3	287.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	872.06	kg/m3	288.15	Study of the binary mixtures of {monoglyme + (hexane, cyclohexane, octane, dodecane)} by ECM-average and PFP models
ρl	872.23	kg/m3	288.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	871.14	kg/m3	289.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	870.05	kg/m3	290.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	868.96	kg/m3	291.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	867.87	kg/m3	292.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	867.00	kg/m3	293.00	KDB
ρl	866.79	kg/m3	293.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	866.71	kg/m3	293.15	Densities and Viscosities of Three Binary Monoglyme + 1-Alcohol Systems from (283.15 to 313.15) K
ρl	865.70	kg/m3	294.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	864.61	kg/m3	295.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	863.51	kg/m3	296.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	862.42	kg/m3	297.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	861.32	kg/m3	298.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	860.40	kg/m3	298.15	Isobaric Vapor Liquid Equilibrium for the Binary Systems of sec-Butyl Acetate + Methyl Ethyl Ketone, 2-Methoxyethanol, or 1,2-Dimethoxyethane at 101.3 kPa
ρl	861.43	kg/m3	298.15	Standard partial molar volumes of some electrolytes in ethylene carbonate based mixtures
ρl	861.20	kg/m3	298.15	Densities and Viscosities of Three Binary Monoglyme + 1-Alcohol Systems from (283.15 to 313.15) K
ρl	861.17	kg/m3	298.15	Study of the binary mixtures of {monoglyme + (hexane, cyclohexane, octane, dodecane)} by ECM-average and PFP models
ρl	860.22	kg/m3	299.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	859.12	kg/m3	300.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	858.01	kg/m3	301.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	856.91	kg/m3	302.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	855.70	kg/m3	303.15	Densities and Viscosities of Three Binary Monoglyme + 1-Alcohol Systems from (283.15 to 313.15) K
ρl	855.80	kg/m3	303.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	854.69	kg/m3	304.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	853.58	kg/m3	305.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	852.46	kg/m3	306.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	851.35	kg/m3	307.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	850.24	kg/m3	308.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	850.13	kg/m3	308.15	Study of the binary mixtures of {monoglyme + (hexane, cyclohexane, octane, dodecane)} by ECM-average and PFP models
ρl	850.28	kg/m3	308.50	Excess Molar Enthalpies and Hydrogen Bonding in Binary Mixtures Containing Ethers and Benzyl Alcohol at 308.15 K and Atmospheric Pressure
ρl	849.13	kg/m3	309.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	848.02	kg/m3	310.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	846.90	kg/m3	311.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	845.79	kg/m3	312.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	844.67	kg/m3	313.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	844.69	kg/m3	313.15	Densities and Viscosities of Three Binary Monoglyme + 1-Alcohol Systems from (283.15 to 313.15) K
ρl	843.55	kg/m3	314.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	842.42	kg/m3	315.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	841.29	kg/m3	316.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	840.17	kg/m3	317.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	839.04	kg/m3	318.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	837.91	kg/m3	319.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	836.77	kg/m3	320.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	835.64	kg/m3	321.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	834.50	kg/m3	322.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	833.36	kg/m3	323.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	832.22	kg/m3	324.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	831.08	kg/m3	325.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	829.93	kg/m3	326.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	828.78	kg/m3	327.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	827.63	kg/m3	328.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	826.48	kg/m3	329.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	825.33	kg/m3	330.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	824.17	kg/m3	331.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	823.02	kg/m3	332.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	821.86	kg/m3	333.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
γ	[0.02; 0.03]	N/m	[278.17; 373.17]
γ	0.03	N/m	278.17	Surface tension of diethyl carbonate, 1,2-dimethoxyethane and diethyl adipate
γ	0.03	N/m	283.17	Surface tension of diethyl carbonate, 1,2-dimethoxyethane and diethyl adipate
γ	0.03	N/m	288.18	Surface tension of diethyl carbonate, 1,2-dimethoxyethane and diethyl adipate
γ	0.02	N/m	293.17	Surface tension of diethyl carbonate, 1,2-dimethoxyethane and diethyl adipate
γ	0.02	N/m	298.03	Surface tension of diethyl carbonate, 1,2-dimethoxyethane and diethyl adipate
γ	0.02	N/m	298.15	Excess Molar Volumes and Surface Tensions of Trimethylbenzene + Ethylene Glycol Ester at 298.15 K and 313.15 K
γ	0.02	N/m	298.15	Excess thermodynamic functions derived from densities and surface tensions of (p- or o-xylene + ethylene glycol dimethyl ether) between the temperatures (298.15 and 308.15) K
γ	0.02	N/m	298.15	Experimental Surface Tensions and Derived Surface Properties of Binary Mixtures of Water + Alkoxyethanols (C1Em, m = 1, 2, 3) and Water + Ethylene Glycol Dimethyl Ether (C1E1C1) at (298.15, 308.15, and 318.15) K
γ	0.02	N/m	303.15	Excess thermodynamic functions derived from densities and surface tensions of (p- or o-xylene + ethylene glycol dimethyl ether) between the temperatures (298.15 and 308.15) K
γ	0.02	N/m	303.15	Surface tension of diethyl carbonate, 1,2-dimethoxyethane and diethyl adipate
γ	0.02	N/m	308.12	Surface tension of diethyl carbonate, 1,2-dimethoxyethane and diethyl adipate
γ	0.02	N/m	308.15	Experimental Surface Tensions and Derived Surface Properties of Binary Mixtures of Water + Alkoxyethanols (C1Em, m = 1, 2, 3) and Water + Ethylene Glycol Dimethyl Ether (C1E1C1) at (298.15, 308.15, and 318.15) K
γ	0.02	N/m	308.15	Excess thermodynamic functions derived from densities and surface tensions of (p- or o-xylene + ethylene glycol dimethyl ether) between the temperatures (298.15 and 308.15) K
γ	0.02	N/m	313.15	Excess Molar Volumes and Surface Tensions of Trimethylbenzene + Ethylene Glycol Ester at 298.15 K and 313.15 K
γ	0.02	N/m	313.16	Surface tension of diethyl carbonate, 1,2-dimethoxyethane and diethyl adipate
γ	0.02	N/m	318.15	Experimental Surface Tensions and Derived Surface Properties of Binary Mixtures of Water + Alkoxyethanols (C1Em, m = 1, 2, 3) and Water + Ethylene Glycol Dimethyl Ether (C1E1C1) at (298.15, 308.15, and 318.15) K
γ	0.02	N/m	318.17	Surface tension of diethyl carbonate, 1,2-dimethoxyethane and diethyl adipate
γ	0.02	N/m	323.18	Surface tension of diethyl carbonate, 1,2-dimethoxyethane and diethyl adipate
γ	0.02	N/m	328.17	Surface tension of diethyl carbonate, 1,2-dimethoxyethane and diethyl adipate
γ	0.02	N/m	333.17	Surface tension of diethyl carbonate, 1,2-dimethoxyethane and diethyl adipate
γ	0.02	N/m	338.17	Surface tension of diethyl carbonate, 1,2-dimethoxyethane and diethyl adipate
γ	0.02	N/m	343.17	Surface tension of diethyl carbonate, 1,2-dimethoxyethane and diethyl adipate
γ	0.02	N/m	348.17	Surface tension of diethyl carbonate, 1,2-dimethoxyethane and diethyl adipate
γ	0.02	N/m	353.18	Surface tension of diethyl carbonate, 1,2-dimethoxyethane and diethyl adipate
γ	0.02	N/m	358.17	Surface tension of diethyl carbonate, 1,2-dimethoxyethane and diethyl adipate
γ	0.02	N/m	363.17	Surface tension of diethyl carbonate, 1,2-dimethoxyethane and diethyl adipate
γ	0.02	N/m	368.17	Surface tension of diethyl carbonate, 1,2-dimethoxyethane and diethyl adipate
γ	0.02	N/m	373.17	Surface tension of diethyl carbonate, 1,2-dimethoxyethane and diethyl adipate
λ	[0.12; 0.16]	W/m×K	[302.75; 392.16]
λ	0.16	W/m×K	302.75	Thermal Conductivity Measurement of Polyglycol Alkyl Ethers at Temperatures from (303.15 to 393.15) K
λ	0.15	W/m×K	332.54	Thermal Conductivity Measurement of Polyglycol Alkyl Ethers at Temperatures from (303.15 to 393.15) K
λ	0.13	W/m×K	362.39	Thermal Conductivity Measurement of Polyglycol Alkyl Ethers at Temperatures from (303.15 to 393.15) K
λ	0.12	W/m×K	392.16	Thermal Conductivity Measurement of Polyglycol Alkyl Ethers at Temperatures from (303.15 to 393.15) K

Datasets

1. Viscosity, Pa*s (1)
2. Mass density, kg/m3 (1)
3. Speed of sound, m/s (1)
4. Thermal conductivity, W/m/K (1)

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
243.15	100.00	0.0009
243.15	4540.00	0.0009
243.15	9560.00	0.0010
243.15	14590.00	0.0010
243.15	19470.00	0.0010
253.15	100.00	0.0007
253.15	4550.00	0.0008
253.15	9550.00	0.0008
253.15	14450.00	0.0008
253.15	19430.00	0.0009
263.15	100.00	0.0006
263.15	4560.00	0.0007
263.15	9590.00	0.0007
263.15	14590.00	0.0007
263.15	19460.00	0.0007
273.15	100.00	0.0006
273.15	4560.00	0.0006
273.15	9590.00	0.0006
273.15	14550.00	0.0006
273.15	19480.00	0.0006
283.15	100.00	0.0005
283.15	4550.00	0.0005
283.15	9570.00	0.0005
283.15	14460.00	0.0005
283.15	19450.00	0.0006
293.15	100.00	0.0004
293.15	4530.00	0.0004
293.15	9560.00	0.0005
293.15	14460.00	0.0005
293.15	19450.00	0.0005
303.15	100.00	0.0004
303.15	4540.00	0.0004
303.15	9500.00	0.0004
303.15	14440.00	0.0004
303.15	19440.00	0.0004
313.15	100.00	0.0004
313.15	4540.00	0.0004
313.15	9500.00	0.0004
313.15	14440.00	0.0004
313.15	19420.00	0.0004
323.15	100.00	0.0003
323.15	4560.00	0.0003
323.15	9530.00	0.0003
323.15	14450.00	0.0004
323.15	19460.00	0.0004
333.15	100.00	0.0003
333.15	4550.00	0.0003
333.15	9570.00	0.0003
333.15	14460.00	0.0003
333.15	19430.00	0.0003
343.15	100.00	0.0003
343.15	4540.00	0.0003
343.15	9560.00	0.0003
343.15	14440.00	0.0003
343.15	19420.00	0.0003
353.15	360.00	0.0002
353.15	4560.00	0.0003
353.15	9570.00	0.0003
353.15	14440.00	0.0003
353.15	19420.00	0.0003
363.15	160.00	0.0002
363.15	4560.00	0.0002
363.15	9570.00	0.0002
363.15	14440.00	0.0003
363.15	19420.00	0.0003
373.15	200.00	0.0002
373.15	4560.00	0.0002
373.15	9580.00	0.0002
373.15	14440.00	0.0002
373.15	19420.00	0.0002
Reference

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.15	100.00	866.7
293.15	5000.00	871.1
293.15	10000.00	875.3
293.15	15000.00	879.5
293.15	20000.00	883.2
293.15	25000.00	887.2
293.15	30000.00	890.9
293.15	35000.00	894.4
293.15	40000.00	897.8
293.15	45000.00	901.1
293.15	50000.00	904.3
293.15	55000.00	907.5
293.15	60000.00	910.4
303.15	100.00	855.5
303.15	5000.00	860.2
303.15	10000.00	864.8
303.15	15000.00	869.2
303.15	20000.00	873.4
303.15	25000.00	877.4
303.15	30000.00	881.3
303.15	35000.00	885.1
303.15	40000.00	888.5
303.15	45000.00	891.9
303.15	50000.00	895.5
303.15	55000.00	898.6
303.15	60000.00	901.7
313.15	100.00	844.4
313.15	5000.00	849.4
313.15	10000.00	854.4
313.15	15000.00	859.1
313.15	20000.00	863.5
313.15	25000.00	867.7
313.15	30000.00	871.7
313.15	35000.00	875.7
313.15	40000.00	879.4
313.15	45000.00	883.1
313.15	50000.00	886.7
313.15	55000.00	890.0
313.15	60000.00	893.3
323.15	100.00	833.1
323.15	5000.00	838.5
323.15	10000.00	843.9
323.15	15000.00	848.7
323.15	20000.00	853.4
323.15	25000.00	858.0
323.15	30000.00	862.3
323.15	35000.00	866.4
323.15	40000.00	870.2
323.15	45000.00	874.2
323.15	50000.00	877.8
323.15	55000.00	881.4
323.15	60000.00	885.0
333.15	100.00	821.6
333.15	5000.00	827.5
333.15	10000.00	833.2
333.15	15000.00	838.7
333.15	20000.00	843.6
333.15	25000.00	848.4
333.15	30000.00	853.1
333.15	35000.00	857.4
333.15	40000.00	861.7
333.15	45000.00	865.6
333.15	50000.00	869.0
333.15	55000.00	873.3
333.15	60000.00	876.7
343.15	100.00	809.9
343.15	5000.00	816.3
343.15	10000.00	822.5
343.15	15000.00	828.3
343.15	20000.00	833.8
343.15	25000.00	838.7
343.15	30000.00	843.5
343.15	35000.00	848.0
343.15	40000.00	852.6
343.15	45000.00	856.6
343.15	50000.00	860.6
343.15	55000.00	864.5
343.15	60000.00	868.3
353.15	100.00	797.6
353.15	5000.00	804.8
353.15	10000.00	811.4
353.15	15000.00	817.6
353.15	20000.00	823.2
353.15	25000.00	828.7
353.15	30000.00	833.8
353.15	35000.00	838.6
353.15	40000.00	843.1
353.15	45000.00	847.8
353.15	50000.00	852.0
353.15	55000.00	856.0
353.15	60000.00	859.8
Reference

Speed of sound, m/s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Speed of sound, m/s - Liquid
293.15	100.00	1188.5
293.15	10000.00	1242.0
293.15	20000.00	1292.4
293.15	30000.00	1336.4
293.15	40000.00	1378.8
293.15	50000.00	1418.2
293.15	60000.00	1455.6
293.15	70000.00	1490.4
293.15	80000.00	1523.9
293.15	90000.00	1555.7
293.15	100000.00	1586.1
303.15	100.00	1144.8
303.15	10000.00	1201.1
303.15	20000.00	1252.2
303.15	30000.00	1299.6
303.15	40000.00	1343.2
303.15	50000.00	1384.1
303.15	60000.00	1422.5
303.15	70000.00	1458.0
303.15	80000.00	1492.6
303.15	90000.00	1525.7
303.15	100000.00	1557.2
313.15	100.00	1101.9
313.15	10000.00	1161.1
313.15	20000.00	1215.2
313.15	30000.00	1263.9
313.15	40000.00	1309.2
313.15	50000.00	1350.7
313.15	60000.00	1390.5
313.15	70000.00	1428.3
313.15	80000.00	1463.3
313.15	90000.00	1497.0
313.15	100000.00	1528.8
323.15	100.00	1059.4
323.15	10000.00	1122.4
323.15	20000.00	1178.7
323.15	30000.00	1229.3
323.15	40000.00	1275.9
323.15	50000.00	1319.6
323.15	60000.00	1361.5
323.15	70000.00	1398.6
323.15	80000.00	1434.7
323.15	90000.00	1468.9
323.15	100000.00	1501.5
333.15	100.00	1016.5
333.15	10000.00	1083.1
333.15	20000.00	1142.7
333.15	30000.00	1195.2
333.15	40000.00	1243.6
333.15	50000.00	1288.4
333.15	60000.00	1330.1
333.15	70000.00	1369.3
333.15	80000.00	1406.4
333.15	90000.00	1441.3
333.15	100000.00	1474.8
343.15	100.00	974.9
343.15	10000.00	1044.7
343.15	20000.00	1107.0
343.15	30000.00	1161.4
343.15	40000.00	1211.6
343.15	50000.00	1257.6
343.15	60000.00	1300.5
343.15	70000.00	1340.5
343.15	80000.00	1378.6
343.15	90000.00	1414.5
343.15	100000.00	1448.7
353.15	100.00	932.8
353.15	10000.00	1005.8
353.15	20000.00	1070.0
353.15	30000.00	1127.3
353.15	40000.00	1178.9
353.15	50000.00	1226.3
353.15	60000.00	1270.4
353.15	70000.00	1311.3
353.15	80000.00	1350.2
353.15	90000.00	1387.0
353.15	100000.00	1421.7
Reference

Thermal conductivity, W/m/K

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Thermal conductivity, W/m/K - Liquid
245.46	104.60	0.1648
245.69	30045.00	0.1742
245.95	9806.60	0.1669
245.96	30102.80	0.1746
246.06	5008.20	0.1665
246.06	20070.20	0.1711
246.24	20007.00	0.1706
246.49	105.90	0.1650
246.52	5028.50	0.1666
246.69	10018.00	0.1683
246.75	10004.90	0.1682
246.79	5010.00	0.1662
247.52	103.30	0.1647
255.91	20016.00	0.1675
256.02	102.50	0.1606
256.02	30007.30	0.1706
256.10	10039.70	0.1643
256.21	5070.20	0.1623
256.75	30013.50	0.1707
256.81	20002.50	0.1679
256.83	10040.40	0.1642
256.90	5065.50	0.1625
256.95	102.50	0.1610
257.48	5064.50	0.1625
257.56	20021.50	0.1674
257.58	102.30	0.1607
257.62	10048.10	0.1643
257.66	30002.00	0.1708
266.15	10002.70	0.1617
266.18	5017.90	0.1601
266.19	30008.80	0.1688
266.26	101.30	0.1580
266.26	20003.00	0.1654
266.32	10010.80	0.1618
266.41	100.90	0.1580
266.58	5037.60	0.1598
266.87	20013.00	0.1650
266.95	30000.50	0.1684
267.11	30012.80	0.1683
267.35	20002.80	0.1653
267.37	10020.80	0.1617
267.50	101.10	0.1578
267.84	5027.00	0.1598
275.68	10023.80	0.1585
275.72	5003.30	0.1567
276.21	20023.80	0.1624
276.34	101.80	0.1547
276.45	30012.00	0.1657
276.49	100.90	0.1543
276.52	20015.00	0.1623
276.94	5006.00	0.1567
277.11	30008.30	0.1654
277.29	10005.30	0.1584
277.31	30011.50	0.1653
277.53	20015.00	0.1623
277.55	5005.50	0.1565
277.95	10000.50	0.1585
278.62	101.10	0.1539
285.80	10010.10	0.1551
286.18	5012.40	0.1531
286.23	101.50	0.1512
286.40	30001.00	0.1626
286.51	20013.30	0.1590
286.67	30008.60	0.1625
286.80	20011.00	0.1590
287.06	101.30	0.1509
287.07	30006.30	0.1621
287.28	10001.10	0.1549
287.46	5010.50	0.1530
287.68	20035.00	0.1586
288.14	10002.40	0.1545
288.62	100.90	0.1504
288.65	5009.10	0.1525
294.52	10025.60	0.1516
294.53	20008.50	0.1566
294.55	30011.50	0.1589
294.64	10026.90	0.1527
294.68	106.80	0.1466
294.68	20035.50	0.1566
294.75	104.20	0.1463
294.83	5021.10	0.1500
294.85	10037.10	0.1514
294.89	30004.50	0.1609
294.98	5020.10	0.1495
295.00	30018.00	0.1595
295.07	5014.00	0.1490
295.11	20026.30	0.1557
295.24	20010.30	0.1569
295.28	30016.00	0.1598
295.32	30006.00	0.1600
295.36	101.90	0.1467
295.36	20005.50	0.1558
295.37	10024.30	0.1515
295.38	104.30	0.1474
295.83	10044.50	0.1522
296.00	5027.10	0.1498
314.60	104.50	0.1394
314.65	105.60	0.1386
314.79	30008.30	0.1522
314.79	30008.30	0.1522
314.83	20003.30	0.1491
314.83	20003.30	0.1491
314.84	5010.30	0.1415
314.87	10003.10	0.1443
314.90	107.10	0.1402
314.95	20015.50	0.1476
314.95	20015.50	0.1476
315.06	10016.70	0.1440
315.14	30009.80	0.1529
315.14	30009.80	0.1529
315.17	10013.20	0.1447
315.17	10013.20	0.1447
315.23	5018.60	0.1424
315.26	30007.80	0.1519
315.26	30007.80	0.1519
315.27	105.40	0.1395
315.30	20008.50	0.1484
315.30	20008.50	0.1484
315.31	20000.80	0.1483
315.31	20000.80	0.1483
315.42	10011.90	0.1445
315.42	10011.90	0.1445
315.46	5010.30	0.1419
315.51	100.60	0.1391
334.53	10005.50	0.1361
334.53	10005.50	0.1361
334.58	102.10	0.1320
334.58	5005.90	0.1342
334.58	102.10	0.1320
334.58	5005.90	0.1342
334.65	5011.80	0.1347
334.65	5011.80	0.1347
334.69	90.00	0.1320
334.69	90.00	0.1320
334.76	10004.20	0.1366
334.76	10004.20	0.1366
334.94	10015.20	0.1373
334.94	10015.20	0.1373
334.98	5008.90	0.1344
334.98	5008.90	0.1344
335.06	101.60	0.1322
335.06	101.60	0.1322
335.31	10008.50	0.1374
335.31	10008.50	0.1374
335.39	5011.50	0.1347
335.39	5011.50	0.1347
335.53	105.60	0.1314
335.53	105.60	0.1314
335.59	10014.80	0.1366
335.59	10014.80	0.1366
335.96	5018.00	0.1343
335.96	5018.00	0.1343
336.14	105.60	0.1319
336.14	105.60	0.1319
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.65]	kPa	[261.38; 381.73]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.47105e+01
Coefficient B			-3.24745e+03
Coefficient C			-3.62220e+01
Temperature range, min.			261.38
Temperature range, max.			381.73
Pvap	1.33	kPa	261.38	Calculated Property
Pvap	2.99	kPa	274.75	Calculated Property
Pvap	6.16	kPa	288.12	Calculated Property
Pvap	11.81	kPa	301.50	Calculated Property
Pvap	21.25	kPa	314.87	Calculated Property
Pvap	36.23	kPa	328.24	Calculated Property
Pvap	58.96	kPa	341.61	Calculated Property
Pvap	92.10	kPa	354.99	Calculated Property
Pvap	138.80	kPa	368.36	Calculated Property
Pvap	202.65	kPa	381.73	Calculated Property
Pvap	[0.03; 3941.47]	kPa	[215.15; 536.15]	KDB Vapor Pressure Data
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			6.14883e+01
Coefficient B			-6.00557e+03
Coefficient C			-6.94194e+00
Coefficient D			5.62976e-06
Temperature range, min.			215.15
Temperature range, max.			536.15
Pvap	0.03	kPa	215.15	Calculated Property
Pvap	0.64	kPa	250.82	Calculated Property
Pvap	5.54	kPa	286.48	Calculated Property
Pvap	28.24	kPa	322.15	Calculated Property
Pvap	100.12	kPa	357.82	Calculated Property
Pvap	275.62	kPa	393.48	Calculated Property
Pvap	632.91	kPa	429.15	Calculated Property
Pvap	1273.37	kPa	464.82	Calculated Property
Pvap	2323.40	kPa	500.48	Calculated Property
Pvap	3941.47	kPa	536.15	Calculated Property

Similar Compounds

Find more compounds similar to Ethane, 1,2-dimethoxy-.

Mixtures

• Ethane, 1,2-dimethoxy- + Water
• Ethane, 1,2-dimethoxy- + 1,3-Dioxolan-2-one
• Ethane, 1,2-dimethoxy- + lithium perchlorate + 1,3-Dioxolan-2-one
• lithium bromide + Ethane, 1,2-dimethoxy- + 1,3-Dioxolan-2-one
• Tetraethylammonium bromide + Ethane, 1,2-dimethoxy- + 1,3-Dioxolan-2-one
• Tetra-N-butylammonium bromide + Ethane, 1,2-dimethoxy- + 1,3-Dioxolan-2-one
• Carbon dioxide + Ethane, 1,2-dimethoxy-
• Ethane, 1,2-dimethoxy- + Heptane
• Decane + Ethane, 1,2-dimethoxy-
• n-Hexane + Ethane, 1,2-dimethoxy-
• Ethane, 1,2-dimethoxy- + Cyclohexane
• Octane + Ethane, 1,2-dimethoxy-
• Dodecane + Ethane, 1,2-dimethoxy-
• Ethane, 1,2-dimethoxy- + Dimethyl Sulfoxide
• p-Xylene + Ethane, 1,2-dimethoxy-
• Ethane, 1,2-dimethoxy- + o-Xylene
• Ethane, 1,2-dimethoxy- + Norflurane
• Ethane, 1,2-dimethoxy- + Nonane
• Ethane, 1,2-dimethoxy- + «beta» Carotene
• Ethane, 1,2-dimethoxy- + Cyclohexane + «beta» Carotene

Find more mixtures with Ethane, 1,2-dimethoxy-.

Sources

• KDB Vapor Pressure Data
• Cheméo Relay (1.0)
• Crippen Method
• Crippen Method
• Temperature and Pressure Dependences of Thermophysical Properties of Some Ethylene Glycol Dimethyl Ethers from Ultrasonic Measurements
• Density and Viscosity Measurements of Dimethoxymethane and 1,2-Dimethoxyethane from 243 K to 373 K up to 20 MPa
• Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
• Bubble temperature measurements on the binary mixtures formed by decane with a variety of compounds at 95.8 kPa
• Temperature dependence of limiting activity coefficients and Henry s law constants of cyclic and open-chain ethers in water
• Vapour liquid equilibria of the system 1,1,1,2-tetrafluoroethane + monoethylene-glycol dimethylether from 283.15 to 353.15 K: New modified UNIFAC parameters
• Surface tension of diethyl carbonate, 1,2-dimethoxyethane and diethyl adipate
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
• Phase equilibria of CO2 + 1,2-dimethoxyethane at high-pressures
• Standard partial molar volumes of some electrolytes in ethylene carbonate based mixtures
• Partial molar volumes of organic solutes in water. XVIII: Selected polyethers(aq) and 3,6-dioxa-1-heptanol(aq) at T = (298 to 573) K and at pressures up to 30 MPa
• Non-ideal behaviour of a room temperature ionic liquid in an alkoxyethanol or poly ethers at T = (298.15 to 318.15) K
• Apparent molar volumes and apparent molar heat capacities of aqueous tetrahydrofuran, dimethyl sulfoxide, 1,4-dioxane, and 1,2-dimethoxyethane at temperatures from 278.15 K to 393.15 K and at the pressure 0.35 MPa
• Efficient determination of crystallisation and melting points at low cooling and heating rates with novel computer controlled equipment
• Study of static permittivity and density of the systems {(n-nonane + monoglyme or diglyme)} at various temperatures
• Excess thermodynamic functions derived from densities and surface tensions of (p- or o-xylene + ethylene glycol dimethyl ether) between the temperatures (298.15 and 308.15) K
• Permittivity and density of the systems (monoglyme, diglyme, triglyme, or tetraglyme + n-heptane) at several temperatures
• Enthalpies of solvation of ethylene oxide oligomers CH3O(CH2CH2O)nCH3 (n = 1 to 4) in different H-bonding solvents: Methanol, chloroform, and water. Group contribution method as applied to the polar oligomers
• Interactions of volatile organic compounds with the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
• Solubilities of some organic solutes in 1-ethyl-3-methylimidazolium acetate. Chromatographic measurements and predictions from COSMO-RS
• Henry s constants and activity coefficients of some organic solutes in 1-butyl,3-methylimidazolium hydrogen sulfate and in 1-methyl,3-trimethylsilylmethylimidazolium chloride
• Interactions of volatile organic compounds with the ionic liquids 1-butyl-1-methylpyrrolidinium tetracyanoborate and 1-butyl-1-methylpyrrolidinium bis(oxalato)borate
• Infinite dilution activity coefficients of volatile organic compounds in two ionic liquids composed of the tris(pentafluoroethyl) trifluorophosphate ([FAP]) anion and a functionalized cation
• Study of the binary mixtures of {monoglyme + (hexane, cyclohexane, octane, dodecane)} by ECM-average and PFP models
• Thermophysical properties of dimethyl sulfoxide + cyclic and linear ethers at 308.15K Application of an extended cell model
• Thermochemical behaviour of straight-chain ethers CH3O(CH2CH2O)nCH3 (n = 1 4) in aqueous and tetrachlormethane solutions
• Isobaric Vapor Liquid Equilibrium for the Binary Systems of sec-Butyl Acetate + Methyl Ethyl Ketone, 2-Methoxyethanol, or 1,2-Dimethoxyethane at 101.3 kPa
• Isobaric Vapor-Liquid Equilibrium Data for Two Binary Systems n-Hexane + 1,2-Dimethoxyethane and Methylcyclopentane + 1,2-Dimethoxyethane at 101.3 kPa
• DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development
• Bubble Temperature Measurements on Binary Mixtures Formed by Cyclohexane at 94.7 kPa
• Solubility of -Carotene in Binary Solvents Formed by Some Hydrocarbons with Dibutyl Ether and 1,2-Dimethoxyethane
• Experimental Surface Tensions and Derived Surface Properties of Binary Mixtures of Water + Alkoxyethanols (C1Em, m = 1, 2, 3) and Water + Ethylene Glycol Dimethyl Ether (C1E1C1) at (298.15, 308.15, and 318.15) K
• Liquid Densities and Refractive Indices of Binary Mixtures for the Dimethyl Ether of a Glycol + Ethanol from T=288.15 K to 318.15 K
• Volumetric Properties of Monoethylene Glycol Dimethyl Ether and Diethylene Glycol Dimethyl Ether up to 60 MPa
• Excess Molar Enthalpies and Hydrogen Bonding in Binary Mixtures Containing Ethers and Benzyl Alcohol at 308.15 K and Atmospheric Pressure
• Excess Molar Volumes and Surface Tensions of Trimethylbenzene + Ethylene Glycol Ester at 298.15 K and 313.15 K
• Enthalpy of Solvation of Monoglyme, Diglyme, Triglyme, Tetraglyme, and Pentaglyme in Mixtures of Water with N,N-Dimethylformamide at 298.15 K
• Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
• Interactions of Volatile Organic Compounds with the Ionic Liquid 1-Butyl-1-methylpyrrolidinium Dicyanamide
• Densities and Viscosities of Three Binary Monoglyme + 1-Alcohol Systems from (283.15 to 313.15) K
• Partial Molar Volumes and Partial Molar Isentropic Compressions of Four Aliphatic Linear Polyethers at Infinite Dilution in Water at Temperatures T = (278 to 343) K and Atmospheric Pressure.
• Viscosity, Density, and Speed of Sound for the Binary Mixtures of Formamide with 2-Methoxyethanol, Acetophenone, Acetonitrile, 1,2-Dimethoxyethane, and Dimethylsulfoxide at Different Temperatures
• Mass Diffusion Coefficients of Oxygenated Fuel Additives in Diesel Oil and in Heptane at T ) (276 to 333) K
• Thermal Conductivity Measurement of Polyglycol Alkyl Ethers at Temperatures from (303.15 to 393.15) K
• Henry s Law Constants of Organic Compounds in Water and n-Octane at T = 293.2 K
• Joback Method
• KDB
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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