Chemical Properties of Ethane, 1,1'-oxybis[2-methoxy- (CAS 111-96-6)

InChI

InChI=1S/C6H14O3/c1-7-3-5-9-6-4-8-2/h3-6H2,1-2H3

InChI Key

SBZXBUIDTXKZTM-UHFFFAOYSA-N

Formula

C6H14O3

SMILES

COCCOCCOC

Molecular Weight¹

134.17

CAS

111-96-6

Other Names

• (2-Methoxyethyl) ether
• .beta.,.beta.-dimethoxy diethyl ether
• 1,1'-Oxybis(2-methoxy)ethane
• 1,1'-oxybis(2-methoxyethane)
• 1,5-dimethoxydiethyl ether
• 2,2'-Oxybisethanol dimethyl ether
• 2,5,8-trioxanonane
• 2-(2-Methoxyethoxy)-1-methoxyethane
• 2-methoxyethyl ether
• 3-oxa-1,5-pentanediol, dimethyl ether
• CH3OCH2CH2OCH2CH2OCH3
• Di(2-Methoxyethyl) ether
• Diethyl glycol dimethyl ether
• Diethylene glycol dimethyl ether
• Diglycol methyl ether
• Dimethoxydiethylene glycol
• Dimethyldigol
• Ethanol, 2,2'-oxybis-, dimethyl ether
• Ether, bis(2-methoxyethyl)
• Glyme-2
• Methyl diglyme
• NSC 59726
• Poly-Solv
• bis(2-methoxyethyl) ether
• diethylene glycol, dimethyl ether
• diglyme
• diglyme (diethylene glycol dimethyl ether)
• dimethyl carbitol
• dimethyldiglycol

• 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).
• T_flash,cc : Flash Point (Closed Cup Method) (K).
• 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_fusH : Enthalpy of fusion at a given temperature (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).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• NFPA Safety : NFPA Safety Rating.
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• 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_gas : Gas thermal conductivity (W/m×K).
• λ_liquid : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• U_Qi : UNIQUAC Qi Parameter.
• U_Ri : UNIQUAC Ri Parameter.
• 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	0.5775		ChemSep v8.3 pure component data Compiled value
PAff	918.80	kJ/mol	NIST
BasG	870.90	kJ/mol	NIST
ΔcH°liquid	-3805.50 ± 0.90	kJ/mol	NIST
μ	1.97	debye	ChemSep v8.3 pure component data Compiled value
Tflash,cc	336.15	K	NCMS SOLV-DB
ΔfG°	-286.00	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	[-524.70; -511.00]	kJ/mol
ΔfH°gas	-511.00	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-511.70	kJ/mol	NIST
ΔfH°gas	-524.70	kJ/mol	NIST
ΔfH°liquid	[-569.40; -556.40]	kJ/mol
ΔfH°liquid	-556.40 ± 0.90	kJ/mol	NIST
ΔfH°liquid	-569.40	kJ/mol	NIST
ΔfusH°	14.86	kJ/mol	Joback Calculated Property
ΔvapH°	[43.14; 48.00]	kJ/mol
ΔvapH°	43.14	kJ/mol	NCMS SOLV-DB
ΔvapH°	48.00 ± 0.60	kJ/mol	NIST
ΔvapH°	44.70	kJ/mol	NIST
IE	9.80	eV	NIST
log10WS	0.88		Aq. Solubility Prediction
logPoct/wat	-0.480		NCMS SOLV-DB
McVol	113.010	ml/mol	McGowan Calculated Property
NFPA Fire	2		NCMS SOLV-DB
NFPA Health	1		NCMS SOLV-DB
NFPA Safety	1		NCMS SOLV-DB
Pc	2860.00	kPa	ChemSep v8.3 pure component data Compiled value
Ptriple	1.01e-05	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[950.90; 951.00]
Inp	951.00		NIST
Inp	950.90		NIST
Inp	950.90		NIST
S°liquid	352.70	J/mol×K	NIST
Tboil	[432.91; 435.20]	K
Tboil	432.91	K	ChemSep v8.3 pure component data Compiled value
Tboil	435.15	K	NCMS SOLV-DB
Tboil	435.20	K	NIST
Tboil	435.15	K	NIST
Tboil	435.00 ± 4.00	K	NIST
Tc	[608.00; 619.70]	K
Tc	619.70	K	DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development
Tc	617.00	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Tc	608.00	K	ChemSep v8.3 pure component data Compiled value
Tfus	[203.15; 209.15]	K
Tfus	209.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	203.15	K	ChemSep v8.3 pure component data Compiled value
Tfus	207.82	K	Aq. Solubility Prediction
Tfus	205.15	K	NCMS SOLV-DB
Tfus	209.15	K	NIST
Tfus	209.10 ± 0.20	K	NIST
Tfus	209.10 ± 0.20	K	NIST
Ttriple	209.11	K	ChemSep v8.3 pure component data Compiled value
UQi	4.58		ChemSep v8.3 pure component data Compiled value
URi	5.23		ChemSep v8.3 pure component data Compiled value
Vc	0.422	m3/kmol	ChemSep v8.3 pure component data Compiled value
Zc	0.2390000		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[274.10; 279.84]	J/mol×K	[298.15; 298.15]
Cp,liquid	277.76	J/mol×K	298.15	NIST
Cp,liquid	279.84	J/mol×K	298.15	NIST
Cp,liquid	274.10	J/mol×K	298.15	NIST
η	[0.0004120; 0.0015200]	Pa×s	[273.15; 363.15]
η	0.0015200	Pa×s	273.15	Density, viscosity and solubility of carbon dioxide in glymes
η	0.0013800	Pa×s	278.15	Density, viscosity and solubility of carbon dioxide in glymes
η	0.0012600	Pa×s	283.15	Density, viscosity and solubility of carbon dioxide in glymes
η	0.0011400	Pa×s	288.15	Density, viscosity and solubility of carbon dioxide in glymes
η	0.0010600	Pa×s	293.15	Density, viscosity and solubility of carbon dioxide in glymes
η	0.0009890	Pa×s	298.15	NCMS SOLV-DB
η	0.0009760	Pa×s	298.15	Density, viscosity and solubility of carbon dioxide in glymes
η	0.0009010	Pa×s	303.15	Density, viscosity and solubility of carbon dioxide in glymes
η	0.0007770	Pa×s	313.15	Density, viscosity and solubility of carbon dioxide in glymes
η	0.0006760	Pa×s	323.15	Density, viscosity and solubility of carbon dioxide in glymes
η	0.0005920	Pa×s	333.15	Density, viscosity and solubility of carbon dioxide in glymes
η	0.0005220	Pa×s	343.15	Density, viscosity and solubility of carbon dioxide in glymes
η	0.0004640	Pa×s	353.15	Density, viscosity and solubility of carbon dioxide in glymes
η	0.0004120	Pa×s	363.15	Density, viscosity and solubility of carbon dioxide in glymes
εr	[7.12; 7.69]		[288.15; 308.15]
εr	7.69		288.15	Permittivity and density of the systems (monoglyme, diglyme, triglyme, or tetraglyme + n-heptane) at several temperatures
εr	7.40		298.15	Permittivity and density of the systems (monoglyme, diglyme, triglyme, or tetraglyme + n-heptane) at several temperatures
εr	7.12		308.15	Permittivity and density of the systems (monoglyme, diglyme, triglyme, or tetraglyme + n-heptane) at several temperatures
ΔfusH	[17.78; 17.80]	kJ/mol	[209.10; 209.10]
ΔfusH	17.78	kJ/mol	209.10	NIST
ΔfusH	17.80	kJ/mol	209.10	NIST
ΔfusH	17.80	kJ/mol	209.10	NIST
ΔfusH	17.80	kJ/mol	209.10	NIST
ΔvapH	[45.40; 47.40]	kJ/mol	[359.50; 402.50]
ΔvapH	47.40	kJ/mol	359.50	NIST
ΔvapH	45.40	kJ/mol	402.50	NIST
Pvap	0.39	kPa	298.15	NCMS SOLV-DB
n0	[1.39680; 1.41198]		[288.15; 318.15]
n0	1.41198		288.15	Study of static permittivity and density of the systems {(n-nonane + monoglyme or diglyme)} at various temperatures
n0	1.41010		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	1.40580		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	1.40753		298.15	Study of static permittivity and density of the systems {(n-nonane + monoglyme or diglyme)} at various temperatures
n0	1.40580		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	1.40570		298.15	Solubility of a-Carotene in Binary Solvents Formed by Some Hydrocarbons with 2,5,8-Trioxanonane, 2-Propanone, and Cyclohexanone
n0	1.40600		298.15	Density, Speed of Sound, and Refractive Index of Aqueous Binary Mixtures of Some Glycol Ethers at T = 298.15 K
n0	1.40600		298.15	NCMS SOLV-DB
n0	1.40321		308.15	Study of static permittivity and density of the systems {(n-nonane + monoglyme or diglyme)} at various temperatures
n0	1.40120		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	1.39680		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	[863.80; 953.70]	kg/m3	[283.15; 373.15]
ρl	953.66	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	953.70	kg/m3	283.15	Thermophysical properties of glycols and glymes
ρl	952.67	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	951.69	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	950.70	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	949.71	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	948.72	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	948.70	kg/m3	288.15	Thermophysical properties of glycols and glymes
ρl	950.20	kg/m3	288.15	Thermophysical properties of glycols and glymes
ρl	947.73	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	946.74	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	945.75	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	944.76	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	943.80	kg/m3	293.15	Thermophysical properties of glycols and glymes
ρl	945.20	kg/m3	293.15	Excess Properties and Spectral Investigation for the Binary System Diethylene Glycol Dimethyl Ether + Water at T = (293.15, 298.15, 303.15, 308.15 and 313.15) K
ρl	943.76	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	945.20	kg/m3	293.15	Thermophysical properties of glycols and glymes
ρl	942.79	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	941.79	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	940.79	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	939.80	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	938.80	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	939.80	kg/m3	298.15	Excess Properties and Spectral Investigation for the Binary System Diethylene Glycol Dimethyl Ether + Water at T = (293.15, 298.15, 303.15, 308.15 and 313.15) K
ρl	938.80	kg/m3	298.15	Thermophysical properties of glycols and glymes
ρl	938.62	kg/m3	298.15	Excess molar enthalpies and volumes of binary mixtures of nonafluorobutylmethylether with ethylene glycol ethers at T = 298.15 K
ρl	940.20	kg/m3	298.15	Thermophysical properties of glycols and glymes
ρl	937.80	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	936.81	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	935.81	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	934.82	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	933.80	kg/m3	303.15	Thermophysical properties of glycols and glymes
ρl	933.82	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	935.00	kg/m3	303.15	Excess Properties and Spectral Investigation for the Binary System Diethylene Glycol Dimethyl Ether + Water at T = (293.15, 298.15, 303.15, 308.15 and 313.15) K
ρl	935.20	kg/m3	303.15	Thermophysical properties of glycols and glymes
ρl	933.98	kg/m3	303.15	Surface tension of four oxygenated fuels: experiment and correlation
ρl	932.82	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	931.82	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	930.82	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	929.83	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	928.83	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	928.80	kg/m3	308.15	Thermophysical properties of glycols and glymes
ρl	930.20	kg/m3	308.15	Thermophysical properties of glycols and glymes
ρl	930.70	kg/m3	308.15	Excess Properties and Spectral Investigation for the Binary System Diethylene Glycol Dimethyl Ether + Water at T = (293.15, 298.15, 303.15, 308.15 and 313.15) K
ρl	928.95	kg/m3	308.15	Surface tension of four oxygenated fuels: experiment and correlation
ρl	927.82	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	926.83	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	925.82	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	924.82	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	923.82	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	925.40	kg/m3	313.15	Excess Properties and Spectral Investigation for the Binary System Diethylene Glycol Dimethyl Ether + Water at T = (293.15, 298.15, 303.15, 308.15 and 313.15) K
ρl	923.80	kg/m3	313.15	Thermophysical properties of glycols and glymes
ρl	923.97	kg/m3	313.15	Surface tension of four oxygenated fuels: experiment and correlation
ρl	925.20	kg/m3	313.15	Thermophysical properties of glycols and glymes
ρl	922.81	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	921.81	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	920.80	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	919.80	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	920.20	kg/m3	318.15	Thermophysical properties of glycols and glymes
ρl	918.79	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	918.94	kg/m3	318.15	Surface tension of four oxygenated fuels: experiment and correlation
ρl	917.78	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	916.78	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	915.77	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	914.75	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	913.75	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	915.20	kg/m3	323.15	Thermophysical properties of glycols and glymes
ρl	913.90	kg/m3	323.15	Surface tension of four oxygenated fuels: experiment and correlation
ρl	913.70	kg/m3	323.15	Thermophysical properties of glycols and glymes
ρl	912.73	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	911.72	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	910.70	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	909.69	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	908.67	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	908.84	kg/m3	328.15	Surface tension of four oxygenated fuels: experiment and correlation
ρl	910.10	kg/m3	328.15	Thermophysical properties of glycols and glymes
ρl	907.65	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	906.63	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	905.62	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	904.60	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	905.00	kg/m3	333.15	Thermophysical properties of glycols and glymes
ρl	903.59	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
ρl	903.60	kg/m3	333.15	Thermophysical properties of glycols and glymes
ρl	903.76	kg/m3	333.15	Surface tension of four oxygenated fuels: experiment and correlation
ρl	899.90	kg/m3	338.15	Thermophysical properties of glycols and glymes
ρl	898.67	kg/m3	338.15	Surface tension of four oxygenated fuels: experiment and correlation
ρl	894.80	kg/m3	343.15	Thermophysical properties of glycols and glymes
ρl	893.40	kg/m3	343.15	Thermophysical properties of glycols and glymes
ρl	893.55	kg/m3	343.15	Surface tension of four oxygenated fuels: experiment and correlation
ρl	889.70	kg/m3	348.15	Thermophysical properties of glycols and glymes
ρl	888.41	kg/m3	348.15	Surface tension of four oxygenated fuels: experiment and correlation
ρl	884.60	kg/m3	353.15	Thermophysical properties of glycols and glymes
ρl	883.24	kg/m3	353.15	Surface tension of four oxygenated fuels: experiment and correlation
ρl	879.40	kg/m3	358.15	Thermophysical properties of glycols and glymes
ρl	878.04	kg/m3	358.15	Surface tension of four oxygenated fuels: experiment and correlation
ρl	872.81	kg/m3	363.15	Surface tension of four oxygenated fuels: experiment and correlation
ρl	874.20	kg/m3	363.15	Thermophysical properties of glycols and glymes
ρl	869.00	kg/m3	368.15	Thermophysical properties of glycols and glymes
ρl	863.80	kg/m3	373.15	Thermophysical properties of glycols and glymes
ΔfusS	[85.10; 85.10]	J/mol×K	[209.10; 209.10]
ΔfusS	85.10	J/mol×K	209.10	NIST
ΔfusS	85.10	J/mol×K	209.10	NIST
γ	[0.02; 0.03]	N/m	[298.15; 318.15]
γ	0.02	N/m	298.15	Volumetric and Surface Properties of Aqueous Mixtures of Polyethers at T = (298.15, 308.15, and 318.15) K
γ	0.03	N/m	298.15	NCMS SOLV-DB
γ	0.03	N/m	308.15	Volumetric and Surface Properties of Aqueous Mixtures of Polyethers at T = (298.15, 308.15, and 318.15) K
γ	0.02	N/m	318.15	Volumetric and Surface Properties of Aqueous Mixtures of Polyethers at T = (298.15, 308.15, and 318.15) K
λliquid	[0.11; 0.15]	W/m×K	[302.75; 392.16]
λliquid	0.15	W/m×K	302.75	Thermal Conductivity Measurement of Polyglycol Alkyl Ethers at Temperatures from (303.15 to 393.15) K
λliquid	0.13	W/m×K	332.54	Thermal Conductivity Measurement of Polyglycol Alkyl Ethers at Temperatures from (303.15 to 393.15) K
λliquid	0.12	W/m×K	362.39	Thermal Conductivity Measurement of Polyglycol Alkyl Ethers at Temperatures from (303.15 to 393.15) K
λliquid	0.11	W/m×K	392.16	Thermal Conductivity Measurement of Polyglycol Alkyl Ethers at Temperatures from (303.15 to 393.15) K

Datasets

1. Mass density, kg/m3 (2)
2. Speed of sound, m/s (1)

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.69	100.00	953.48
283.69	1000.00	954.15
283.69	5000.00	956.94
283.68	10000.00	960.29
283.68	20000.00	966.68
283.68	30000.00	972.8
283.67	40000.00	978.49
283.67	60000.00	989.12
283.67	80000.00	998.75
283.67	100000.00	1007.71
303.47	100.00	933.69
303.47	1000.00	934.43
303.48	5000.00	937.55
303.48	10000.00	941.31
322.62	30000.00	938.31
322.62	40000.00	945.16
322.62	60000.00	957.74
322.62	80000.00	968.98
322.62	100000.00	979.2
342.49	100.00	894.03
342.49	1000.00	894.98
342.49	5000.00	898.96
342.50	10000.00	903.66
342.50	20000.00	912.57
342.51	30000.00	920.68
342.51	40000.00	928.18
342.51	60000.00	941.77
342.51	80000.00	953.82
303.49	20000.00	948.42
303.49	30000.00	955.17
303.49	40000.00	961.41
303.49	60000.00	973.02
303.50	80000.00	983.33
303.50	100000.00	992.97
322.62	100.00	914.41
322.62	1000.00	915.3
322.62	5000.00	918.77
322.62	10000.00	923.02
322.62	20000.00	930.99
342.52	100000.00	964.68
362.51	100.00	873.45
362.51	1000.00	874.46
362.51	5000.00	879.02
362.52	10000.00	884.41
362.52	20000.00	894.33
362.52	30000.00	903.29
362.52	40000.00	911.53
362.53	60000.00	926.3
362.53	80000.00	939.26
362.53	100000.00	950.89
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.15	100.00	943.5
293.15	5000.00	947.3
293.15	10000.00	950.9
293.15	15000.00	954.4
293.15	20000.00	957.7
293.15	25000.00	960.9
293.15	30000.00	964.0
293.15	35000.00	967.0
293.15	40000.00	969.8
293.15	45000.00	972.8
293.15	50000.00	975.4
293.15	55000.00	978.2
293.15	60000.00	980.9
303.15	100.00	933.7
303.15	5000.00	937.6
303.15	10000.00	941.1
303.15	15000.00	945.0
303.15	20000.00	948.4
303.15	25000.00	951.8
303.15	30000.00	955.2
303.15	35000.00	958.2
303.15	40000.00	961.1
303.15	45000.00	964.0
303.15	50000.00	967.3
303.15	55000.00	970.1
303.15	60000.00	973.2
313.15	100.00	923.7
313.15	5000.00	927.9
313.15	10000.00	931.8
313.15	15000.00	935.7
313.15	20000.00	939.4
313.15	25000.00	942.6
313.15	30000.00	946.5
313.15	35000.00	949.7
313.15	40000.00	952.8
313.15	45000.00	956.1
313.15	50000.00	958.8
313.15	55000.00	961.9
313.15	60000.00	964.9
323.15	100.00	913.7
323.15	5000.00	918.2
323.15	10000.00	922.7
323.15	15000.00	926.4
323.15	20000.00	930.5
323.15	25000.00	934.2
323.15	30000.00	937.6
323.15	35000.00	941.0
323.15	40000.00	944.4
323.15	45000.00	947.6
323.15	50000.00	951.0
323.15	55000.00	953.9
323.15	60000.00	956.7
333.15	100.00	903.6
333.15	5000.00	908.3
333.15	10000.00	912.8
333.15	15000.00	917.3
333.15	20000.00	921.0
333.15	25000.00	925.3
333.15	30000.00	928.9
333.15	35000.00	932.6
333.15	40000.00	936.4
333.15	45000.00	939.8
333.15	50000.00	942.9
333.15	55000.00	946.0
333.15	60000.00	949.1
343.15	100.00	893.6
343.15	5000.00	898.5
343.15	10000.00	903.2
343.15	15000.00	907.8
343.15	20000.00	912.3
343.15	25000.00	916.2
343.15	30000.00	920.5
343.15	35000.00	924.2
343.15	40000.00	928.0
343.15	45000.00	931.4
343.15	50000.00	934.8
343.15	55000.00	938.2
343.15	60000.00	941.4
353.15	100.00	883.3
353.15	5000.00	888.7
353.15	10000.00	893.9
353.15	15000.00	898.7
353.15	20000.00	903.2
353.15	25000.00	907.6
353.15	30000.00	911.6
353.15	35000.00	915.5
353.15	40000.00	919.5
353.15	45000.00	923.1
353.15	50000.00	927.0
353.15	55000.00	930.4
353.15	60000.00	933.6
Reference

Speed of sound, m/s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Speed of sound, m/s - Liquid
293.15	100.00	1298.9
293.15	10000.00	1344.9
293.15	20000.00	1386.5
293.15	30000.00	1426.6
293.15	40000.00	1463.9
293.15	50000.00	1499.2
293.15	60000.00	1532.5
293.15	70000.00	1565.1
293.15	80000.00	1595.5
293.15	90000.00	1624.9
293.15	100000.00	1653.4
303.15	100.00	1259.3
303.15	10000.00	1306.7
303.15	20000.00	1350.6
303.15	30000.00	1392.0
303.15	40000.00	1430.4
303.15	50000.00	1466.9
303.15	60000.00	1501.5
303.15	70000.00	1534.3
303.15	80000.00	1565.8
303.15	90000.00	1595.9
303.15	100000.00	1625.1
313.15	100.00	1219.9
313.15	10000.00	1269.5
313.15	20000.00	1315.4
313.15	30000.00	1357.6
313.15	40000.00	1397.8
313.15	50000.00	1435.3
313.15	60000.00	1470.5
313.15	70000.00	1504.4
313.15	80000.00	1536.7
313.15	90000.00	1567.6
313.15	100000.00	1597.0
323.15	100.00	1180.9
323.15	10000.00	1232.5
323.15	20000.00	1280.2
323.15	30000.00	1324.4
323.15	40000.00	1365.5
323.15	50000.00	1404.0
323.15	60000.00	1440.6
323.15	70000.00	1475.2
323.15	80000.00	1508.2
323.15	90000.00	1539.8
323.15	100000.00	1569.9
333.15	100.00	1142.4
333.15	10000.00	1196.4
333.15	20000.00	1246.0
333.15	30000.00	1291.4
333.15	40000.00	1333.7
333.15	50000.00	1373.6
333.15	60000.00	1410.9
333.15	70000.00	1446.2
333.15	80000.00	1480.1
333.15	90000.00	1512.3
333.15	100000.00	1543.1
343.15	100.00	1104.2
343.15	10000.00	1160.8
343.15	20000.00	1212.0
343.15	30000.00	1259.5
343.15	40000.00	1303.1
343.15	50000.00	1343.9
343.15	60000.00	1382.1
343.15	70000.00	1418.6
343.15	80000.00	1452.9
343.15	90000.00	1485.9
343.15	100000.00	1517.4
353.15	100.00	1066.6
353.15	10000.00	1125.7
353.15	20000.00	1179.3
353.15	30000.00	1228.1
353.15	40000.00	1273.4
353.15	50000.00	1314.9
353.15	60000.00	1354.4
353.15	70000.00	1391.3
353.15	80000.00	1426.7
353.15	90000.00	1460.4
353.15	100000.00	1492.3
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[153.53; 443.80]	J/mol×K	[255.00; 1500.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K
Coefficient A			8.39897e+01
Coefficient B			-5.05000e+02
Coefficient C			6.22224e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			255.00
Temperature range, max.			1500.00
Cp,gas	153.53	J/mol×K	255.00	Calculated Property
Cp,gas	223.53	J/mol×K	393.33	Calculated Property
Cp,gas	278.87	J/mol×K	531.67	Calculated Property
Cp,gas	321.10	J/mol×K	670.00	Calculated Property
Cp,gas	353.74	J/mol×K	808.33	Calculated Property
Cp,gas	379.53	J/mol×K	946.67	Calculated Property
Cp,gas	400.33	J/mol×K	1085.00	Calculated Property
Cp,gas	417.42	J/mol×K	1223.33	Calculated Property
Cp,gas	431.70	J/mol×K	1361.67	Calculated Property
Cp,gas	443.80	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[270.67; 293.96]	J/mol×K	[209.11; 400.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,liquid in J/mol×K, T in K
Coefficient A			3.18270e+02
Coefficient B			-4.10400e-01
Coefficient C			8.74080e-04
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			209.11
Temperature range, max.			400.00
Cp,liquid	270.67	J/mol×K	209.11	Calculated Property
Cp,liquid	270.11	J/mol×K	230.32	Calculated Property
Cp,liquid	270.34	J/mol×K	251.53	Calculated Property
Cp,liquid	271.36	J/mol×K	272.74	Calculated Property
Cp,liquid	273.16	J/mol×K	293.95	Calculated Property
Cp,liquid	275.75	J/mol×K	315.16	Calculated Property
Cp,liquid	279.12	J/mol×K	336.37	Calculated Property
Cp,liquid	283.28	J/mol×K	357.58	Calculated Property
Cp,liquid	288.23	J/mol×K	378.79	Calculated Property
Cp,liquid	293.96	J/mol×K	400.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0071309; 0.0002235]	Pa×s	[209.11; 435.65]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-1.14410e+01
Coefficient B			1.38550e+03
Coefficient C			-2.39600e-02
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			209.11
Temperature range, max.			435.65
η	0.0071309	Pa×s	209.11	Calculated Property
η	0.0034898	Pa×s	234.28	Calculated Property
η	0.0019614	Pa×s	259.45	Calculated Property
η	0.0012204	Pa×s	284.62	Calculated Property
η	0.0008201	Pa×s	309.79	Calculated Property
η	0.0005849	Pa×s	334.97	Calculated Property
η	0.0004373	Pa×s	360.14	Calculated Property
η	0.0003396	Pa×s	385.31	Calculated Property
η	0.0002720	Pa×s	410.48	Calculated Property
η	0.0002235	Pa×s	435.65	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[57.37; 0.00]	kJ/mol	[209.11; 608.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K
Coefficient A			6.69560e+01
Coefficient B			3.66520e-01
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Critical temperature, Tc (K)			6.08000e+02
Temperature range, min.			209.11
Temperature range, max.			608.00
ΔvapH	57.37	kJ/mol	209.11	Calculated Property
ΔvapH	54.95	kJ/mol	253.43	Calculated Property
ΔvapH	52.32	kJ/mol	297.75	Calculated Property
ΔvapH	49.45	kJ/mol	342.07	Calculated Property
ΔvapH	46.25	kJ/mol	386.39	Calculated Property
ΔvapH	42.62	kJ/mol	430.72	Calculated Property
ΔvapH	38.36	kJ/mol	475.04	Calculated Property
ΔvapH	33.06	kJ/mol	519.36	Calculated Property
ΔvapH	25.64	kJ/mol	563.68	Calculated Property
ΔvapH	0.00	kJ/mol	608.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.67]	kPa	[322.72; 461.92]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.56921e+01
Coefficient B			-4.43052e+03
Coefficient C			-3.51090e+01
Temperature range, min.			322.72
Temperature range, max.			461.92
Pvap	1.33	kPa	322.72	Calculated Property
Pvap	2.93	kPa	338.19	Calculated Property
Pvap	5.95	kPa	353.65	Calculated Property
Pvap	11.33	kPa	369.12	Calculated Property
Pvap	20.38	kPa	384.59	Calculated Property
Pvap	34.88	kPa	400.05	Calculated Property
Pvap	57.14	kPa	415.52	Calculated Property
Pvap	90.06	kPa	430.99	Calculated Property
Pvap	137.18	kPa	446.45	Calculated Property
Pvap	202.67	kPa	461.92	Calculated Property
Pvap	[1.01e-05; 2860.48]	kPa	[209.11; 608.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K
Coefficient A			1.70262e+02
Coefficient B			-1.16300e+04
Coefficient C			-2.45070e+01
Coefficient D			2.28930e-02
Coefficient E			1.00000e+00
Temperature range, min.			209.11
Temperature range, max.			608.00
Pvap	1.01e-05	kPa	209.11	Calculated Property
Pvap	4.19e-03	kPa	253.43	Calculated Property
Pvap	0.21	kPa	297.75	Calculated Property
Pvap	2.99	kPa	342.07	Calculated Property
Pvap	20.58	kPa	386.39	Calculated Property
Pvap	87.80	kPa	430.72	Calculated Property
Pvap	272.79	kPa	475.04	Calculated Property
Pvap	683.05	kPa	519.36	Calculated Property
Pvap	1472.94	kPa	563.68	Calculated Property
Pvap	2860.48	kPa	608.00	Calculated Property
Pvap	[0.13; 101.22]	kPa	[286.00; 433.00]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.58239e+01
Coefficient B			-4.42588e+03
Coefficient C			-3.80630e+01
Reference			Stull, 1947
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			286.00
Temperature range, max.			433.00
Pvap	0.13	kPa	286.00	Calculated Property
Pvap	0.40	kPa	302.33	Calculated Property
Pvap	1.05	kPa	318.67	Calculated Property
Pvap	2.51	kPa	335.00	Calculated Property
Pvap	5.45	kPa	351.33	Calculated Property
Pvap	10.98	kPa	367.67	Calculated Property
Pvap	20.70	kPa	384.00	Calculated Property
Pvap	36.85	kPa	400.33	Calculated Property
Pvap	62.42	kPa	416.67	Calculated Property
Pvap	101.22	kPa	433.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[1029.26; 317.96]	kg/m3	[209.11; 608.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K
Coefficient A			8.28028e+01
Coefficient B			2.60420e-01
Coefficient C			6.08000e+02
Coefficient D			3.22060e-01
Temperature range, min.			209.11
Temperature range, max.			608.00
ρl	1029.26	kg/m3	209.11	Calculated Property
ρl	985.23	kg/m3	253.43	Calculated Property
ρl	939.42	kg/m3	297.75	Calculated Property
ρl	891.40	kg/m3	342.07	Calculated Property
ρl	840.51	kg/m3	386.39	Calculated Property
ρl	785.72	kg/m3	430.72	Calculated Property
ρl	725.27	kg/m3	475.04	Calculated Property
ρl	655.63	kg/m3	519.36	Calculated Property
ρl	567.25	kg/m3	563.68	Calculated Property
ρl	317.96	kg/m3	608.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 0.01]	N/m	[205.15; 435.15]	Jasper (1972), surface tension of pure liquid compounds Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is γ in N/m, T in K
Coefficient A			6.42647e-02
Coefficient B			-1.16400e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			205.15
Temperature range, max.			435.15
γ	0.04	N/m	205.15	Calculated Property
γ	0.04	N/m	230.71	Calculated Property
γ	0.03	N/m	256.26	Calculated Property
γ	0.03	N/m	281.82	Calculated Property
γ	0.03	N/m	307.37	Calculated Property
γ	0.03	N/m	332.93	Calculated Property
γ	0.02	N/m	358.48	Calculated Property
γ	0.02	N/m	384.04	Calculated Property
γ	0.02	N/m	409.59	Calculated Property
γ	0.01	N/m	435.15	Calculated Property
γ	[0.04; 0.00]	N/m	[209.11; 608.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is γ in N/m, T in K
Coefficient A			7.58460e-02
Coefficient B			1.35690e+00
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Critical temperature, Tc (K)			6.08000e+02
Temperature range, min.			209.11
Temperature range, max.			608.00
γ	0.04	N/m	209.11	Calculated Property
γ	0.04	N/m	253.43	Calculated Property
γ	0.03	N/m	297.75	Calculated Property
γ	0.02	N/m	342.07	Calculated Property
γ	0.02	N/m	386.39	Calculated Property
γ	0.01	N/m	430.72	Calculated Property
γ	0.01	N/m	475.04	Calculated Property
γ	0.01	N/m	519.36	Calculated Property
γ	0.00	N/m	563.68	Calculated Property
γ	0.00	N/m	608.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.02; 0.07]	W/m×K	[435.65; 1000.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K
Coefficient A			1.70430e-04
Coefficient B			9.49650e-01
Coefficient C			7.23210e+02
Coefficient D			0.00000e+00
Temperature range, min.			435.65
Temperature range, max.			1000.00
λgas	0.02	W/m×K	435.65	Calculated Property
λgas	0.03	W/m×K	498.36	Calculated Property
λgas	0.03	W/m×K	561.06	Calculated Property
λgas	0.04	W/m×K	623.77	Calculated Property
λgas	0.04	W/m×K	686.47	Calculated Property
λgas	0.05	W/m×K	749.18	Calculated Property
λgas	0.05	W/m×K	811.88	Calculated Property
λgas	0.06	W/m×K	874.59	Calculated Property
λgas	0.06	W/m×K	937.29	Calculated Property
λgas	0.07	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.17; 0.10]	W/m×K	[209.11; 573.15]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is λliquid in W/m×K, T in K
Coefficient A			2.15960e-01
Coefficient B			-1.96560e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			209.11
Temperature range, max.			573.15
λliquid	0.17	W/m×K	209.11	Calculated Property
λliquid	0.17	W/m×K	249.56	Calculated Property
λliquid	0.16	W/m×K	290.01	Calculated Property
λliquid	0.15	W/m×K	330.46	Calculated Property
λliquid	0.14	W/m×K	370.91	Calculated Property
λliquid	0.14	W/m×K	411.35	Calculated Property
λliquid	0.13	W/m×K	451.80	Calculated Property
λliquid	0.12	W/m×K	492.25	Calculated Property
λliquid	0.11	W/m×K	532.70	Calculated Property
λliquid	0.10	W/m×K	573.15	Calculated Property

Similar Compounds

Find more compounds similar to Ethane, 1,1'-oxybis[2-methoxy-.

Mixtures

• Ethane, fluoro- + Ethane, 1,1'-oxybis[2-methoxy-
• Ethane, 1,1'-oxybis[2-methoxy- + Heptane
• Carbon dioxide + Ethane, 1,1'-oxybis[2-methoxy-
• Methane, difluoro- + Ethane, 1,1'-oxybis[2-methoxy-
• Ethane, 1,1'-oxybis[2-methoxy- + Ethane, 1,1-difluoro-
• Ethane, 1,1'-oxybis[2-methoxy- + 1,1,1,3,3-Pentafluoropropane (R245fa)
• Ethane, 1,1'-oxybis[2-methoxy- + Nonane
• Ethanol + Ethane, 1,1'-oxybis[2-methoxy-
• Ethane, 1,1'-oxybis[2-methoxy- + Norflurane
• Ethane, 1,1'-oxybis[2-methoxy- + 1-Butanol
• Ethane, 1,1'-oxybis[2-methoxy- + Ethane, 1,2-dichloro-
• Ethane, 1,1'-oxybis[2-methoxy- + Water
• Ethane, 1,1'-oxybis[2-methoxy- + Propane, 1,1,1,3,3,3-hexafluoro-
• Ethane, 1,1'-oxybis[2-methoxy- + Cyclohexane + «beta» Carotene
• n-Hexane + Ethane, 1,1'-oxybis[2-methoxy- + «beta» Carotene
• Toluene + Ethane, 1,1'-oxybis[2-methoxy- + «beta» Carotene
• 1-Hexene + Ethane, 1,1'-oxybis[2-methoxy- + «beta» Carotene
• Methane + Ethane, 1,1'-oxybis[2-methoxy-
• Ethane + Ethane, 1,1'-oxybis[2-methoxy-

Sources

• Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
• IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 ChEDL chemicals 1.5.2, from Kudchadker, A. P.; Ambrose, D.; Tsonopoulos, C. Vapor-Liquid Critical Properties of Elements and Compounds. 7. Oxygen Compounds Other Than Alkanols and Cycloalkanols. J. Chem. Eng. Data 2001, 46, 457-479.
• Jasper (1972), surface tension of pure liquid compounds ChEDL chemicals 1.5.2, from Jasper, J. J. The Surface Tension of Pure Liquid Compounds. J. Phys. Chem. Ref. Data 1972, 1, 841-1010 (as transcribed in Lange's Handbook).
• ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
• Temperature and Pressure Dependences of Thermophysical Properties of Some Ethylene Glycol Dimethyl Ethers from Ultrasonic Measurements
• Density, viscosity and solubility of carbon dioxide in glymes
• Vapor-liquid equilibria of difluoromethane + N,N-dimethylacetamide, difluoromethane + dimethylether diethylene glycol and 1,1-difluoroethane + dimethylether diethylene glycol systems
• Vapor-liquid equilibrium measurement of1,1,1,3,3-pentafluoropropane + N,N-dimethylformamide/diethyleneglycol dimethyl ether/N-methyl-2-pyrrolidone working fluids forabsorption power cycle
• Surface tension of four oxygenated fuels: experiment and correlation
• Excess molar enthalpies and volumes of binary mixtures of nonafluorobutylmethylether with ethylene glycol ethers at T = 298.15 K
• 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
• Study of static permittivity and density of the systems {(n-nonane + monoglyme or diglyme)} at various temperatures
• 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
• Sync-measurement experimental study of (fluoroethane + dimethylether tetraethylene glycol), (fluoroethane + dimethylether triethylene glycol) and (fluoroethane + dimethylether diethylene glycol) systems
• Thermochemical behaviour of straight-chain ethers CH3O(CH2CH2O)nCH3 (n = 1 4) in aqueous and tetrachlormethane solutions
• Effect of properties of the N,N-dimethylformamide-methanol and N,N-dimethylformamide-water mixtures on the solution enthalpy of glymes in these mixtures at 298.15 K
• Thermophysical properties of glycols and glymes
• Isothermal Vapor Liquid Equilibrium of HFC-161 + DMETrEG within the Temperature Range of 293.15 353.15 K and Comparison for HFC-161 Combined with Different Absorbents
• Compressed Liquid Densities of Binary Mixtures of 1-Butanol and Diethylene Glycol Dimethyl Ether from (283 to 363) K at Pressures up to 100 MPa
• DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development
• 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
• Solubility Study of Methane and Ethane In Promising Physical Solvents for Natural Gas Sweetening Operations
• Solubility of a-Carotene in Binary Solvents Formed by Some Hydrocarbons with 2,5,8-Trioxanonane, 2-Propanone, and Cyclohexanone
• Enthalpy of Solvation of Monoglyme, Diglyme, Triglyme, Tetraglyme, and Pentaglyme in Mixtures of Water with N,N-Dimethylformamide at 298.15 K
• Volumetric and Surface Properties of Aqueous Mixtures of Polyethers at T = (298.15, 308.15, and 318.15) K
• Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
• Excess Properties and Spectral Investigation for the Binary System Diethylene Glycol Dimethyl Ether + Water at T = (293.15, 298.15, 303.15, 308.15 and 313.15) K
• Measurement and Correlation of Isothermal Vapor Liquid Equilibrium of 1,1,1,3,3-Pentafluoropropane + N,N-Dimethylacetamide and 1,1,1,3,3,3-Hexafluoropropane + N,N-Dimethylacetamide/Diethylene Glycol Dimethyl Ether Systems
• 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.
• 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
• p-T-x Measurements for Some Working Fluids for an Absorption Heat Transformer: 1,1,1,2-Tetrafluoroethane (R134a) + Dimethylether Diethylene Glycol (DMEDEG) and Dimethylether Triethylene Glycol (DMETrEG)
• Density, Speed of Sound, and Refractive Index of Aqueous Binary Mixtures of Some Glycol Ethers at T = 298.15 K
• Joback Method
• Aqueous Solubility Prediction Method
• McGowan Method
• NIST Webbook
• NCMS SOLV-DB
• The Yaws Handbook of Vapor Pressure

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