Chemical Properties of 2,5,8,11,14-Pentaoxapentadecane (CAS 143-24-8)

InChI

InChI=1S/C10H22O5/c1-11-3-5-13-7-9-15-10-8-14-6-4-12-2/h3-10H2,1-2H3

InChI Key

ZUHZGEOKBKGPSW-UHFFFAOYSA-N

Formula

C10H22O5

SMILES

COCCOCCOCCOCCOC

Molecular Weight¹

222.28

CAS

143-24-8

Other Names

• Ansul Ether 181AT
• Bis[2-(2-methoxyethoxy)ethyl] ether
• CH3O[CH2CH2O]4CH3
• E 181 (ether)
• Ether, bis[2-(2-methoxyethoxy)ethyl]
• Glyme-5
• NSC 65624
• Nissan Uniox MM 200
• Tetraethylene glycol dimethyl ether
• bis(2-(2-methoxyethoxy)ethyl) ether
• dimethoxytetraethylene glycol
• dimethoxytetraglycol
• tetraethylene glycol, dimethyl ether
• tetraglyme

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• BasG : Gas basicity (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_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_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• 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	0.9652		ChemSep v8.3 pure component data Compiled value
PAff	953.80	kJ/mol	NIST
BasG	897.80	kJ/mol	NIST
μ	2.47	debye	ChemSep v8.3 pure component data Compiled value
ΔfG°	-503.00	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-884.00	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfusH°	27.60	kJ/mol	Joback Calculated Property
ΔvapH°	76.90 ± 2.60	kJ/mol	NIST
IE	9.49	eV	Relay (1.0) Calculated Property
log10WS	-0.13		Relay (1.0) Calculated Property
logPoct/wat	0.329		Crippen Calculated Property
McVol	181.110	ml/mol	McGowan Calculated Property
Pc	1940.00	kPa	ChemSep v8.3 pure component data Compiled value
Ptriple	3.14e-07	kPa	ChemSep v8.3 pure component data Compiled value
Tboil	[548.15; 549.00]	K
Tboil	548.95	K	ChemSep v8.3 pure component data Compiled value
Tboil	549.00	K	NIST
Tboil	548.15	K	NIST
Tc	[705.00; 726.60]	K
Tc	726.60	K	DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development
Tc	705.00	K	ChemSep v8.3 pure component data Compiled value
Tfus	[243.15; 243.45]	K
Tfus	243.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	243.45	K	ChemSep v8.3 pure component data Compiled value
Tfus	243.45	K	NIST
Ttriple	243.45	K	ChemSep v8.3 pure component data Compiled value
UQi	7.22		ChemSep v8.3 pure component data Compiled value
URi	8.42		ChemSep v8.3 pure component data Compiled value
Vc	0.674	m3/kmol	ChemSep v8.3 pure component data Compiled value
Zc	0.2230000		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	457.10	J/mol×K	298.15	NIST
η	[0.0011000; 0.0069800]	Pa×s	[273.15; 363.15]
η	0.0069800	Pa×s	273.15	Density, viscosity and solubility of carbon dioxide in glymes
η	0.0059100	Pa×s	278.15	Density, viscosity and solubility of carbon dioxide in glymes
η	0.0050600	Pa×s	283.15	Density, viscosity and solubility of carbon dioxide in glymes
η	0.0043700	Pa×s	288.15	Density, viscosity and solubility of carbon dioxide in glymes
η	0.0038400	Pa×s	293.15	Density, viscosity and solubility of carbon dioxide in glymes
η	0.0033800	Pa×s	298.15	Densities, Viscosities, and Derived Functions of Binary Mixtures: (Tetraethylene Glycol Dimethyl Ether + Water) from 298.15 K to 343.15 K
η	0.0034000	Pa×s	298.15	Density, viscosity and solubility of carbon dioxide in glymes
η	0.0029900	Pa×s	303.15	Density, viscosity and solubility of carbon dioxide in glymes
η	0.0024500	Pa×s	313.15	Density, viscosity and solubility of carbon dioxide in glymes
η	0.0024200	Pa×s	313.15	Densities, Viscosities, and Derived Functions of Binary Mixtures: (Tetraethylene Glycol Dimethyl Ether + Water) from 298.15 K to 343.15 K
η	0.0020200	Pa×s	323.15	Density, viscosity and solubility of carbon dioxide in glymes
η	0.0020040	Pa×s	323.15	Densities, Viscosities, and Derived Functions of Binary Mixtures: (Tetraethylene Glycol Dimethyl Ether + Water) from 298.15 K to 343.15 K
η	0.0017000	Pa×s	333.15	Density, viscosity and solubility of carbon dioxide in glymes
η	0.0016900	Pa×s	333.15	Densities, Viscosities, and Derived Functions of Binary Mixtures: (Tetraethylene Glycol Dimethyl Ether + Water) from 298.15 K to 343.15 K
η	0.0014500	Pa×s	343.15	Density, viscosity and solubility of carbon dioxide in glymes
η	0.0014200	Pa×s	343.15	Densities, Viscosities, and Derived Functions of Binary Mixtures: (Tetraethylene Glycol Dimethyl Ether + Water) from 298.15 K to 343.15 K
η	0.0012600	Pa×s	353.15	Density, viscosity and solubility of carbon dioxide in glymes
η	0.0011000	Pa×s	363.15	Density, viscosity and solubility of carbon dioxide in glymes
εr	[7.55; 8.04]		[288.15; 308.15]
εr	8.04		288.15	Permittivity and density of the systems (monoglyme, diglyme, triglyme, or tetraglyme + n-heptane) at several temperatures
εr	7.78		298.15	Permittivity and density of the systems (monoglyme, diglyme, triglyme, or tetraglyme + n-heptane) at several temperatures
εr	7.55		308.15	Permittivity and density of the systems (monoglyme, diglyme, triglyme, or tetraglyme + n-heptane) at several temperatures
ΔvapH	58.00	kJ/mol	486.00	NIST
n0	[1.42210; 1.43440]		[288.15; 318.15]
n0	1.43440		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	1.43260		293.15	DIELECTRIC AND REFRACTIVE INDEX MEASUREMENTS FOR THE SYSTEMS 1-PENTANOL + 2,5,8,11,14-PENTAOXAPENTADECANE, OR FOR 2,5,8,11,14-PENTAOXAPENTADECANE + OCTANE AT (293.15-303.15) K.
n0	1.43060		298.15	DIELECTRIC AND REFRACTIVE INDEX MEASUREMENTS FOR THE SYSTEMS 1-PENTANOL + 2,5,8,11,14-PENTAOXAPENTADECANE, OR FOR 2,5,8,11,14-PENTAOXAPENTADECANE + OCTANE AT (293.15-303.15) K.
n0	1.43030		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	1.42860		303.15	DIELECTRIC AND REFRACTIVE INDEX MEASUREMENTS FOR THE SYSTEMS 1-PENTANOL + 2,5,8,11,14-PENTAOXAPENTADECANE, OR FOR 2,5,8,11,14-PENTAOXAPENTADECANE + OCTANE AT (293.15-303.15) K.
n0	1.42620		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	1.42210		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	[938.90; 1020.70]	kg/m3	[283.15; 373.15]
ρl	1020.70	kg/m3	283.15	Thermophysical properties of glycols and glymes
ρl	1020.30	kg/m3	283.15	The Viscosity and Density of Ionic Liquid + Tetraglyme Mixtures and the Effect of Tetraglyme on CO2 Solubility
ρl	1016.70	kg/m3	288.15	Volumetric and viscometric behavior of the binary systems ethyl lactate + 1,2- propanediol, + 1,3-propanediol, + tetrahydrofuran and + tetraethylene glycol dimethyl ether. New UNIFAC-VISCO and ASOG-VISCO parameters determination
ρl	1017.00	kg/m3	288.15	Thermophysical properties of glycols and glymes
ρl	1016.10	kg/m3	288.15	Thermophysical properties of glycols and glymes
ρl	1015.60	kg/m3	288.15	The Viscosity and Density of Ionic Liquid + Tetraglyme Mixtures and the Effect of Tetraglyme on CO2 Solubility
ρl	1015.63	kg/m3	288.15	Volumetric Properties, Viscosities, and Refractive Indices of the Binary Systems 1-Butanol + PEG 200, + PEG 400, and + TEGDME
ρl	1015.63	kg/m3	288.15	Volumetric and Viscometric Behavior of Binary Systems 2-Butanol + PEG 200, + PEG 400, + Tetraethylene Glycol Dimethyl Ether, and + N-Methyl-2-pyrrolidone
ρl	1015.63	kg/m3	288.15	Volumetric and viscometric properties of binary liquid mixtures as potential solvents for flue gas desulfurization processes
ρl	1015.86	kg/m3	288.15	On permittivity and density of the systems (tetraglyme + dimethyl or diethyl carbonate) and the formulation of De in terms of volume or mole fraction
ρl	1011.00	kg/m3	293.15	The Viscosity and Density of Ionic Liquid + Tetraglyme Mixtures and the Effect of Tetraglyme on CO2 Solubility
ρl	1012.30	kg/m3	293.15	Thermophysical properties of glycols and glymes
ρl	1012.06	kg/m3	293.15	Volumetric and viscometric behavior of the binary systems ethyl lactate + 1,2- propanediol, + 1,3-propanediol, + tetrahydrofuran and + tetraethylene glycol dimethyl ether. New UNIFAC-VISCO and ASOG-VISCO parameters determination
ρl	1011.00	kg/m3	293.15	Volumetric and viscometric properties of binary liquid mixtures as potential solvents for flue gas desulfurization processes
ρl	1011.50	kg/m3	293.15	Thermophysical properties of glycols and glymes
ρl	1011.00	kg/m3	293.15	Volumetric Properties, Viscosities, and Refractive Indices of the Binary Systems 1-Butanol + PEG 200, + PEG 400, and + TEGDME
ρl	1011.00	kg/m3	293.15	Volumetric and Viscometric Behavior of Binary Systems 2-Butanol + PEG 200, + PEG 400, + Tetraethylene Glycol Dimethyl Ether, and + N-Methyl-2-pyrrolidone
ρl	1009.20	kg/m3	295.15	The Viscosity and Density of Ionic Liquid + Tetraglyme Mixtures and the Effect of Tetraglyme on CO2 Solubility
ρl	1007.42	kg/m3	298.15	Volumetric and viscometric behavior of the binary systems ethyl lactate + 1,2- propanediol, + 1,3-propanediol, + tetrahydrofuran and + tetraethylene glycol dimethyl ether. New UNIFAC-VISCO and ASOG-VISCO parameters determination
ρl	1007.12	kg/m3	298.15	Thermodynamics of Mixtures Containing Ethers. Part III. Liquid-Liquid Equilibria for 2,5,8,11-Tetraoxadodecane or 2,5,8,11,14-Pentaoxapentadecane + Selected N-Alkanes
ρl	1006.36	kg/m3	298.15	Volumetric Properties, Viscosities, and Refractive Indices of the Binary Systems 1-Butanol + PEG 200, + PEG 400, and + TEGDME
ρl	1006.36	kg/m3	298.15	Volumetric and Viscometric Behavior of Binary Systems 2-Butanol + PEG 200, + PEG 400, + Tetraethylene Glycol Dimethyl Ether, and + N-Methyl-2-pyrrolidone
ρl	1006.80	kg/m3	298.15	Thermophysical properties of glycols and glymes
ρl	1006.20	kg/m3	298.15	Liquid-Liquid Equilibrium of Ternary Mixtures Formed by Some Oligooxaethylenes with Ethanol and Hexadecane
ρl	1006.40	kg/m3	298.15	The Viscosity and Density of Ionic Liquid + Tetraglyme Mixtures and the Effect of Tetraglyme on CO2 Solubility
ρl	1006.36	kg/m3	298.15	Volumetric and viscometric properties of binary liquid mixtures as potential solvents for flue gas desulfurization processes
ρl	1007.60	kg/m3	298.15	Thermophysical properties of glycols and glymes
ρl	1007.16	kg/m3	298.15	On permittivity and density of the systems (tetraglyme + dimethyl or diethyl carbonate) and the formulation of De in terms of volume or mole fraction
ρl	1001.73	kg/m3	303.15	Volumetric and Viscometric Behavior of Binary Systems 2-Butanol + PEG 200, + PEG 400, + Tetraethylene Glycol Dimethyl Ether, and + N-Methyl-2-pyrrolidone
ρl	1001.73	kg/m3	303.15	Volumetric and viscometric properties of binary liquid mixtures as potential solvents for flue gas desulfurization processes
ρl	1001.73	kg/m3	303.15	Volumetric Properties, Viscosities, and Refractive Indices of the Binary Systems 1-Butanol + PEG 200, + PEG 400, and + TEGDME
ρl	1002.20	kg/m3	303.15	Thermophysical properties of glycols and glymes
ρl	1001.80	kg/m3	303.15	The Viscosity and Density of Ionic Liquid + Tetraglyme Mixtures and the Effect of Tetraglyme on CO2 Solubility
ρl	1002.79	kg/m3	303.15	Volumetric and viscometric behavior of the binary systems ethyl lactate + 1,2- propanediol, + 1,3-propanediol, + tetrahydrofuran and + tetraethylene glycol dimethyl ether. New UNIFAC-VISCO and ASOG-VISCO parameters determination
ρl	1003.10	kg/m3	303.15	Thermophysical properties of glycols and glymes
ρl	997.10	kg/m3	308.15	Volumetric and Viscometric Behavior of Binary Systems 2-Butanol + PEG 200, + PEG 400, + Tetraethylene Glycol Dimethyl Ether, and + N-Methyl-2-pyrrolidone
ρl	997.60	kg/m3	308.15	Thermophysical properties of glycols and glymes
ρl	998.80	kg/m3	308.15	Thermophysical properties of glycols and glymes
ρl	997.43	kg/m3	308.15	On permittivity and density of the systems (tetraglyme + dimethyl or diethyl carbonate) and the formulation of De in terms of volume or mole fraction
ρl	997.10	kg/m3	308.15	Volumetric and viscometric properties of binary liquid mixtures as potential solvents for flue gas desulfurization processes
ρl	997.20	kg/m3	308.15	The Viscosity and Density of Ionic Liquid + Tetraglyme Mixtures and the Effect of Tetraglyme on CO2 Solubility
ρl	998.15	kg/m3	308.15	Volumetric and viscometric behavior of the binary systems ethyl lactate + 1,2- propanediol, + 1,3-propanediol, + tetrahydrofuran and + tetraethylene glycol dimethyl ether. New UNIFAC-VISCO and ASOG-VISCO parameters determination
ρl	997.10	kg/m3	308.15	Volumetric Properties, Viscosities, and Refractive Indices of the Binary Systems 1-Butanol + PEG 200, + PEG 400, and + TEGDME
ρl	992.48	kg/m3	313.15	Volumetric Properties, Viscosities, and Refractive Indices of the Binary Systems 1-Butanol + PEG 200, + PEG 400, and + TEGDME
ρl	993.00	kg/m3	313.15	Thermophysical properties of glycols and glymes
ρl	992.48	kg/m3	313.15	Volumetric and viscometric properties of binary liquid mixtures as potential solvents for flue gas desulfurization processes
ρl	992.48	kg/m3	313.15	Volumetric and Viscometric Behavior of Binary Systems 2-Butanol + PEG 200, + PEG 400, + Tetraethylene Glycol Dimethyl Ether, and + N-Methyl-2-pyrrolidone
ρl	993.52	kg/m3	313.15	Volumetric and viscometric behavior of the binary systems ethyl lactate + 1,2- propanediol, + 1,3-propanediol, + tetrahydrofuran and + tetraethylene glycol dimethyl ether. New UNIFAC-VISCO and ASOG-VISCO parameters determination
ρl	992.60	kg/m3	313.15	The Viscosity and Density of Ionic Liquid + Tetraglyme Mixtures and the Effect of Tetraglyme on CO2 Solubility
ρl	994.10	kg/m3	313.15	Thermophysical properties of glycols and glymes
ρl	987.93	kg/m3	318.15	On permittivity and density of the systems (tetraglyme + dimethyl or diethyl carbonate) and the formulation of De in terms of volume or mole fraction
ρl	987.86	kg/m3	318.15	Volumetric and viscometric properties of binary liquid mixtures as potential solvents for flue gas desulfurization processes
ρl	987.86	kg/m3	318.15	Volumetric Properties, Viscosities, and Refractive Indices of the Binary Systems 1-Butanol + PEG 200, + PEG 400, and + TEGDME
ρl	989.50	kg/m3	318.15	Thermophysical properties of glycols and glymes
ρl	987.86	kg/m3	318.15	Volumetric and Viscometric Behavior of Binary Systems 2-Butanol + PEG 200, + PEG 400, + Tetraethylene Glycol Dimethyl Ether, and + N-Methyl-2-pyrrolidone
ρl	988.00	kg/m3	318.15	The Viscosity and Density of Ionic Liquid + Tetraglyme Mixtures and the Effect of Tetraglyme on CO2 Solubility
ρl	988.89	kg/m3	318.15	Volumetric and viscometric behavior of the binary systems ethyl lactate + 1,2- propanediol, + 1,3-propanediol, + tetrahydrofuran and + tetraethylene glycol dimethyl ether. New UNIFAC-VISCO and ASOG-VISCO parameters determination
ρl	984.26	kg/m3	323.15	Volumetric and viscometric behavior of the binary systems ethyl lactate + 1,2- propanediol, + 1,3-propanediol, + tetrahydrofuran and + tetraethylene glycol dimethyl ether. New UNIFAC-VISCO and ASOG-VISCO parameters determination
ρl	983.70	kg/m3	323.15	Thermophysical properties of glycols and glymes
ρl	984.90	kg/m3	323.15	Thermophysical properties of glycols and glymes
ρl	983.40	kg/m3	323.15	The Viscosity and Density of Ionic Liquid + Tetraglyme Mixtures and the Effect of Tetraglyme on CO2 Solubility
ρl	983.23	kg/m3	323.15	Volumetric Properties, Viscosities, and Refractive Indices of the Binary Systems 1-Butanol + PEG 200, + PEG 400, and + TEGDME
ρl	983.23	kg/m3	323.15	Volumetric and viscometric properties of binary liquid mixtures as potential solvents for flue gas desulfurization processes
ρl	983.23	kg/m3	323.15	Volumetric and Viscometric Behavior of Binary Systems 2-Butanol + PEG 200, + PEG 400, + Tetraethylene Glycol Dimethyl Ether, and + N-Methyl-2-pyrrolidone
ρl	979.31	kg/m3	328.15	On permittivity and density of the systems (tetraglyme + dimethyl or diethyl carbonate) and the formulation of De in terms of volume or mole fraction
ρl	978.80	kg/m3	328.15	The Viscosity and Density of Ionic Liquid + Tetraglyme Mixtures and the Effect of Tetraglyme on CO2 Solubility
ρl	978.61	kg/m3	328.15	Volumetric Properties, Viscosities, and Refractive Indices of the Binary Systems 1-Butanol + PEG 200, + PEG 400, and + TEGDME
ρl	978.61	kg/m3	328.15	Volumetric and viscometric properties of binary liquid mixtures as potential solvents for flue gas desulfurization processes
ρl	980.20	kg/m3	328.15	Thermophysical properties of glycols and glymes
ρl	975.60	kg/m3	333.15	Thermophysical properties of glycols and glymes
ρl	974.20	kg/m3	333.15	The Viscosity and Density of Ionic Liquid + Tetraglyme Mixtures and the Effect of Tetraglyme on CO2 Solubility
ρl	973.99	kg/m3	333.15	Volumetric and viscometric properties of binary liquid mixtures as potential solvents for flue gas desulfurization processes
ρl	974.50	kg/m3	333.15	Thermophysical properties of glycols and glymes
ρl	973.99	kg/m3	333.15	Volumetric Properties, Viscosities, and Refractive Indices of the Binary Systems 1-Butanol + PEG 200, + PEG 400, and + TEGDME
ρl	971.00	kg/m3	338.15	Thermophysical properties of glycols and glymes
ρl	969.60	kg/m3	338.15	The Viscosity and Density of Ionic Liquid + Tetraglyme Mixtures and the Effect of Tetraglyme on CO2 Solubility
ρl	965.30	kg/m3	343.15	Thermophysical properties of glycols and glymes
ρl	965.00	kg/m3	343.15	The Viscosity and Density of Ionic Liquid + Tetraglyme Mixtures and the Effect of Tetraglyme on CO2 Solubility
ρl	966.50	kg/m3	343.15	Thermophysical properties of glycols and glymes
ρl	960.40	kg/m3	348.15	The Viscosity and Density of Ionic Liquid + Tetraglyme Mixtures and the Effect of Tetraglyme on CO2 Solubility
ρl	961.90	kg/m3	348.15	Thermophysical properties of glycols and glymes
ρl	955.80	kg/m3	353.15	The Viscosity and Density of Ionic Liquid + Tetraglyme Mixtures and the Effect of Tetraglyme on CO2 Solubility
ρl	957.30	kg/m3	353.15	Thermophysical properties of glycols and glymes
ρl	952.70	kg/m3	358.15	Thermophysical properties of glycols and glymes
ρl	948.10	kg/m3	363.15	Thermophysical properties of glycols and glymes
ρl	943.50	kg/m3	368.15	Thermophysical properties of glycols and glymes
ρl	938.90	kg/m3	373.15	Thermophysical properties of glycols and glymes
γ	[0.03; 0.03]	N/m	[298.15; 318.15]
γ	0.03	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	308.15	Volumetric and Surface Properties of Aqueous Mixtures of Polyethers at T = (298.15, 308.15, and 318.15) K
γ	0.03	N/m	318.15	Volumetric and Surface Properties of Aqueous Mixtures of Polyethers at T = (298.15, 308.15, and 318.15) K
λliquid	[0.13; 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	0.14	W/m×K	332.54	Thermal Conductivity Measurement of Polyglycol Alkyl Ethers at Temperatures from (303.15 to 393.15) K
λliquid	0.13	W/m×K	362.39	Thermal Conductivity Measurement of Polyglycol Alkyl Ethers at Temperatures from (303.15 to 393.15) K
λliquid	0.13	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 (1)
2. Speed of sound, m/s (1)

Mass density, kg/m3

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
100.00	278.15	1025.1
100.00	283.15	1020.4
100.00	293.15	1011.1
100.00	303.15	1002.1
100.00	313.15	992.9
100.00	323.15	983.6
100.00	333.15	974.1
100.00	343.15	965.0
100.00	353.15	955.7
1000.00	278.15	1025.6
1000.00	283.15	1020.9
1000.00	293.15	1011.6
1000.00	303.15	1002.7
1000.00	313.15	993.5
1000.00	323.15	984.3
1000.00	333.15	974.8
1000.00	343.15	965.8
1000.00	353.15	956.5
2500.00	278.15	1026.5
2500.00	283.15	1021.8
2500.00	293.15	1012.6
2500.00	303.15	1003.7
2500.00	313.15	994.6
2500.00	323.15	985.3
2500.00	333.15	976.0
2500.00	343.15	967.0
2500.00	353.15	957.8
5000.00	278.15	1027.9
5000.00	283.15	1023.3
5000.00	293.15	1014.1
5000.00	303.15	1005.3
5000.00	313.15	996.3
5000.00	323.15	987.1
5000.00	333.15	977.9
5000.00	343.15	969.0
5000.00	353.15	959.9
7500.00	278.15	1029.3
7500.00	283.15	1024.7
7500.00	293.15	1015.6
7500.00	303.15	1006.9
7500.00	313.15	997.9
7500.00	323.15	988.9
7500.00	333.15	979.8
7500.00	343.15	971.0
7500.00	353.15	962.0
10000.00	278.15	1030.7
10000.00	283.15	1026.1
10000.00	293.15	1017.1
10000.00	303.15	1008.5
10000.00	313.15	999.6
10000.00	323.15	990.6
10000.00	333.15	981.6
10000.00	343.15	972.9
10000.00	353.15	964.0
15000.00	278.15	1033.4
15000.00	283.15	1028.9
15000.00	293.15	1020.0
15000.00	303.15	1011.5
15000.00	313.15	1002.8
15000.00	323.15	994.0
15000.00	333.15	985.1
15000.00	343.15	976.6
15000.00	353.15	967.9
20000.00	278.15	1036.1
20000.00	283.15	1031.6
20000.00	293.15	1022.9
20000.00	303.15	1014.5
20000.00	313.15	1006.0
20000.00	323.15	997.3
20000.00	333.15	988.5
20000.00	343.15	980.2
20000.00	353.15	971.7
25000.00	278.15	1038.7
25000.00	283.15	1034.3
25000.00	293.15	1025.6
25000.00	303.15	1017.4
25000.00	313.15	1009.0
25000.00	323.15	1000.5
25000.00	333.15	991.8
25000.00	343.15	983.7
25000.00	353.15	975.3
Reference

Speed of sound, m/s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Speed of sound, m/s - Liquid
293.15	100.00	1400.2
293.15	10000.00	1439.3
293.15	20000.00	1477.3
293.15	30000.00	1512.3
293.15	40000.00	1546.2
293.15	50000.00	1578.2
293.15	60000.00	1609.1
293.15	70000.00	1638.4
293.15	80000.00	1666.8
293.15	90000.00	1694.2
293.15	100000.00	1720.6
303.15	100.00	1361.6
303.15	10000.00	1402.8
303.15	20000.00	1441.7
303.15	30000.00	1478.2
303.15	40000.00	1513.0
303.15	50000.00	1546.1
303.15	60000.00	1577.7
303.15	70000.00	1607.6
303.15	80000.00	1637.0
303.15	90000.00	1664.9
303.15	100000.00	1692.0
313.15	100.00	1324.5
313.15	10000.00	1367.0
313.15	20000.00	1407.3
313.15	30000.00	1444.9
313.15	40000.00	1480.9
313.15	50000.00	1514.8
313.15	60000.00	1547.2
313.15	70000.00	1578.1
313.15	80000.00	1607.8
313.15	90000.00	1636.4
313.15	100000.00	1663.9
323.15	100.00	1288.0
323.15	10000.00	1332.1
323.15	20000.00	1373.8
323.15	30000.00	1412.5
323.15	40000.00	1449.5
323.15	50000.00	1484.2
323.15	60000.00	1517.4
323.15	70000.00	1548.8
323.15	80000.00	1579.3
323.15	90000.00	1608.6
323.15	100000.00	1636.7
333.15	100.00	1252.0
333.15	10000.00	1297.9
333.15	20000.00	1340.7
333.15	30000.00	1380.8
333.15	40000.00	1418.3
333.15	50000.00	1454.2
333.15	60000.00	1488.4
333.15	70000.00	1520.7
333.15	80000.00	1551.9
333.15	90000.00	1581.5
333.15	100000.00	1610.2
343.15	100.00	1216.6
343.15	10000.00	1264.2
343.15	20000.00	1308.6
343.15	30000.00	1349.9
343.15	40000.00	1388.8
343.15	50000.00	1425.3
343.15	60000.00	1460.1
343.15	70000.00	1493.1
343.15	80000.00	1524.7
343.15	90000.00	1555.3
343.15	100000.00	1584.4
353.15	100.00	1181.6
353.15	10000.00	1231.2
353.15	20000.00	1276.9
353.15	30000.00	1319.8
353.15	40000.00	1359.8
353.15	50000.00	1397.1
353.15	60000.00	1432.8
353.15	70000.00	1466.5
353.15	80000.00	1498.9
353.15	90000.00	1529.8
353.15	100000.00	1559.5
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[247.41; 712.09]	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			1.33826e+02
Coefficient B			-5.00000e+02
Coefficient C			6.69336e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			255.00
Temperature range, max.			1500.00
Cp,gas	247.41	J/mol×K	255.00	Calculated Property
Cp,gas	360.20	J/mol×K	393.33	Calculated Property
Cp,gas	448.94	J/mol×K	531.67	Calculated Property
Cp,gas	516.47	J/mol×K	670.00	Calculated Property
Cp,gas	568.59	J/mol×K	808.33	Calculated Property
Cp,gas	609.72	J/mol×K	946.67	Calculated Property
Cp,gas	642.87	J/mol×K	1085.00	Calculated Property
Cp,gas	670.10	J/mol×K	1223.33	Calculated Property
Cp,gas	692.84	J/mol×K	1361.67	Calculated Property
Cp,gas	712.09	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0244348; 0.0001741]	Pa×s	[243.45; 564.00]	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			4.29350e+01
Coefficient B			-2.18010e+03
Coefficient C			-7.55450e+00
Coefficient D			1.34170e+10
Coefficient E			-4.00000e+00
Temperature range, min.			243.45
Temperature range, max.			564.00
η	0.0244348	Pa×s	243.45	Calculated Property
η	0.0054742	Pa×s	279.07	Calculated Property
η	0.0022999	Pa×s	314.68	Calculated Property
η	0.0012841	Pa×s	350.30	Calculated Property
η	0.0008243	Pa×s	385.92	Calculated Property
η	0.0005696	Pa×s	421.53	Calculated Property
η	0.0004105	Pa×s	457.15	Calculated Property
η	0.0003036	Pa×s	492.77	Calculated Property
η	0.0002284	Pa×s	528.38	Calculated Property
η	0.0001741	Pa×s	564.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[77.18; 0.00]	kJ/mol	[243.45; 705.00]	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			8.63800e+01
Coefficient B			2.65800e-01
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Critical temperature, Tc (K)			7.05000e+02
Temperature range, min.			243.45
Temperature range, max.			705.00
ΔvapH	77.18	kJ/mol	243.45	Calculated Property
ΔvapH	74.80	kJ/mol	294.73	Calculated Property
ΔvapH	72.19	kJ/mol	346.02	Calculated Property
ΔvapH	69.30	kJ/mol	397.30	Calculated Property
ΔvapH	66.02	kJ/mol	448.58	Calculated Property
ΔvapH	62.22	kJ/mol	499.87	Calculated Property
ΔvapH	57.64	kJ/mol	551.15	Calculated Property
ΔvapH	51.75	kJ/mol	602.43	Calculated Property
ΔvapH	43.04	kJ/mol	653.72	Calculated Property
ΔvapH	0.00	kJ/mol	705.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.64]	kPa	[419.76; 578.51]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.70035e+01
Coefficient B			-6.17570e+03
Coefficient C			-5.03140e+01
Temperature range, min.			419.76
Temperature range, max.			578.51
Pvap	1.33	kPa	419.76	Calculated Property
Pvap	2.86	kPa	437.40	Calculated Property
Pvap	5.72	kPa	455.04	Calculated Property
Pvap	10.82	kPa	472.68	Calculated Property
Pvap	19.45	kPa	490.32	Calculated Property
Pvap	33.41	kPa	507.95	Calculated Property
Pvap	55.13	kPa	525.59	Calculated Property
Pvap	87.76	kPa	543.23	Calculated Property
Pvap	135.30	kPa	560.87	Calculated Property
Pvap	202.64	kPa	578.51	Calculated Property
Pvap	[3.14e-07; 1977.35]	kPa	[243.45; 705.00]	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			6.11462e+01
Coefficient B			-1.06480e+04
Coefficient C			-5.89330e+00
Coefficient D			1.59830e-18
Coefficient E			6.00000e+00
Temperature range, min.			243.45
Temperature range, max.			705.00
Pvap	3.14e-07	kPa	243.45	Calculated Property
Pvap	2.06e-04	kPa	294.73	Calculated Property
Pvap	0.02	kPa	346.02	Calculated Property
Pvap	0.40	kPa	397.30	Calculated Property
Pvap	4.21	kPa	448.58	Calculated Property
Pvap	25.70	kPa	499.87	Calculated Property
Pvap	107.01	kPa	551.15	Calculated Property
Pvap	338.59	kPa	602.43	Calculated Property
Pvap	878.52	kPa	653.72	Calculated Property
Pvap	1977.35	kPa	705.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[1057.86; 329.79]	kg/m3	[243.45; 705.00]	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			8.52084e+01
Coefficient B			2.58370e-01
Coefficient C			7.05000e+02
Coefficient D			3.52700e-01
Temperature range, min.			243.45
Temperature range, max.			705.00
ρl	1057.86	kg/m3	243.45	Calculated Property
ρl	1008.86	kg/m3	294.73	Calculated Property
ρl	958.28	kg/m3	346.02	Calculated Property
ρl	905.69	kg/m3	397.30	Calculated Property
ρl	850.46	kg/m3	448.58	Calculated Property
ρl	791.62	kg/m3	499.87	Calculated Property
ρl	727.48	kg/m3	551.15	Calculated Property
ρl	654.70	kg/m3	602.43	Calculated Property
ρl	564.23	kg/m3	653.72	Calculated Property
ρl	329.79	kg/m3	705.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 0.00]	N/m	[243.45; 705.00]	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			6.88700e-02
Coefficient B			1.31550e+00
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Critical temperature, Tc (K)			7.05000e+02
Temperature range, min.			243.45
Temperature range, max.			705.00
γ	0.04	N/m	243.45	Calculated Property
γ	0.03	N/m	294.73	Calculated Property
γ	0.03	N/m	346.02	Calculated Property
γ	0.02	N/m	397.30	Calculated Property
γ	0.02	N/m	448.58	Calculated Property
γ	0.01	N/m	499.87	Calculated Property
γ	0.01	N/m	551.15	Calculated Property
γ	0.01	N/m	602.43	Calculated Property
γ	0.00	N/m	653.72	Calculated Property
γ	0.00	N/m	705.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.02; 0.06]	W/m×K	[548.95; 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			1.71090e-04
Coefficient B			9.18000e-01
Coefficient C			7.62190e+02
Coefficient D			0.00000e+00
Temperature range, min.			548.95
Temperature range, max.			1000.00
λgas	0.02	W/m×K	548.95	Calculated Property
λgas	0.03	W/m×K	599.07	Calculated Property
λgas	0.03	W/m×K	649.18	Calculated Property
λgas	0.03	W/m×K	699.30	Calculated Property
λgas	0.04	W/m×K	749.42	Calculated Property
λgas	0.04	W/m×K	799.53	Calculated Property
λgas	0.04	W/m×K	849.65	Calculated Property
λgas	0.05	W/m×K	899.77	Calculated Property
λgas	0.05	W/m×K	949.88	Calculated Property
λgas	0.06	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.15; 0.09]	W/m×K	[243.45; 548.95]	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			2.02200e-01
Coefficient B			-2.08700e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			243.45
Temperature range, max.			548.95
λliquid	0.15	W/m×K	243.45	Calculated Property
λliquid	0.14	W/m×K	277.39	Calculated Property
λliquid	0.14	W/m×K	311.34	Calculated Property
λliquid	0.13	W/m×K	345.28	Calculated Property
λliquid	0.12	W/m×K	379.23	Calculated Property
λliquid	0.12	W/m×K	413.17	Calculated Property
λliquid	0.11	W/m×K	447.12	Calculated Property
λliquid	0.10	W/m×K	481.06	Calculated Property
λliquid	0.09	W/m×K	515.01	Calculated Property
λliquid	0.09	W/m×K	548.95	Calculated Property

Similar Compounds

Find more compounds similar to 2,5,8,11,14-Pentaoxapentadecane.

Mixtures

• 2,5,8,11,14-Pentaoxapentadecane + Nonane
• Dodecane + 2,5,8,11,14-Pentaoxapentadecane
• Ethane, fluoro- + 2,5,8,11,14-Pentaoxapentadecane
• 2,5,8,11,14-Pentaoxapentadecane + Norflurane
• 2,5,8,11,14-Pentaoxapentadecane + Heptane
• Carbonic acid, dimethyl ester + 2,5,8,11,14-Pentaoxapentadecane
• Diethyl carbonate + 2,5,8,11,14-Pentaoxapentadecane
• 2,5,8,11,14-Pentaoxapentadecane + LACTIC ACID, ETHYL ESTER
• 2,5,8,11,14-Pentaoxapentadecane + 1-Pentanol
• 2,5,8,11,14-Pentaoxapentadecane + Octane
• 1,2-Ethanediol + 2,5,8,11,14-Pentaoxapentadecane + Sulfur dioxide
• Carbon dioxide + 2,5,8,11,14-Pentaoxapentadecane
• 2,5,8,11,14-Pentaoxapentadecane + 1-Butanol
• Ethanol + 2,5,8,11,14-Pentaoxapentadecane
• helium + 2,5,8,11,14-Pentaoxapentadecane
• neon + 2,5,8,11,14-Pentaoxapentadecane
• 2,5,8,11,14-Pentaoxapentadecane + Argon
• 2,5,8,11,14-Pentaoxapentadecane + Krypton
• Xenon + 2,5,8,11,14-Pentaoxapentadecane
• Hydrogen + 2,5,8,11,14-Pentaoxapentadecane

Find more mixtures with 2,5,8,11,14-Pentaoxapentadecane.

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).
• Cheméo Relay (1.0)
• 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.
• Crippen Method
• Crippen Method
• Volumetric Properties, Viscosities, and Refractive Indices of the Binary Systems 1-Butanol + PEG 200, + PEG 400, and + TEGDME
• Viscosity measurements and correlations of binary mixtures: 1,1,1,2-tetrafluoroethane (HFC-134a) + tetraethylene glycol dimethylether (TEGDME)
• Density, viscosity and solubility of carbon dioxide in glymes
• Volumetric and viscometric behavior of the binary systems ethyl lactate + 1,2- propanediol, + 1,3-propanediol, + tetrahydrofuran and + tetraethylene glycol dimethyl ether. New UNIFAC-VISCO and ASOG-VISCO parameters determination
• Solubility of dilute sulfur dioxide in binary mixtures of ethylene glycol and tetraethylene glycol dimethyl ether
• On the permittivity and density of the systems {tetraglyme + (n-nonane or n-dodecane)} at various temperatures
• On permittivity and density of the systems (tetraglyme + dimethyl or diethyl carbonate) and the formulation of De in terms of volume or mole fraction
• 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
• Partial molar volumes of organic solutes in water. XXVII. Two aliphatic polyethers (triglyme, tetraglyme) at temperatures T = 298 573 K and pressures up to 30 MPa
• Volumetric and viscometric properties of binary liquid mixtures as potential solvents for flue gas desulfurization processes
• Thermochemical behaviour of straight-chain ethers CH3O(CH2CH2O)nCH3 (n = 1 4) in aqueous and tetrachlormethane solutions
• DIELECTRIC AND REFRACTIVE INDEX MEASUREMENTS FOR THE SYSTEMS 1-PENTANOL + 2,5,8,11,14-PENTAOXAPENTADECANE, OR FOR 2,5,8,11,14-PENTAOXAPENTADECANE + OCTANE AT (293.15-303.15) K.
• 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
• The Viscosity and Density of Ionic Liquid + Tetraglyme Mixtures and the Effect of Tetraglyme on CO2 Solubility
• DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development
• Solubility Measurement and Thermodynamic Properties Calculation for Several CO2 + Ether Absorbent Systems
• Solubilities of Nonpolar Gases in Triethylene Glycol Dimethyl Ether, Tetraethylene Glycol Dimethyl Ether, Dimethyl Carbonate, and Diethyl Carbonate at 298.15 K and 101.33 kPa Partial Pressure of Gas
• 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
• Thermophysical properties of two PAG-derivative lubricants from high pressure acoustic measurements
• Volumetric Properties of Binary Tetraethylene Glycol Dimethyl Ether + Heptane Mixtures between (278.15 and 353.15) K and up to 25 MPa
• Densities, Viscosities, and Derived Functions of Binary Mixtures: (Tetraethylene Glycol Dimethyl Ether + Water) from 298.15 K to 343.15 K
• Thermodynamics of Mixtures Containing Ethers. Part III. Liquid-Liquid Equilibria for 2,5,8,11-Tetraoxadodecane or 2,5,8,11,14-Pentaoxapentadecane + Selected N-Alkanes
• Solubility Study of Methane and Ethane In Promising Physical Solvents for Natural Gas Sweetening Operations
• 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 and Viscometric Behavior of Binary Systems 2-Butanol + PEG 200, + PEG 400, + Tetraethylene Glycol Dimethyl Ether, and + N-Methyl-2-pyrrolidone
• 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.
• Liquid-Liquid Equilibrium of Ternary Mixtures Formed by Some Oligooxaethylenes with Ethanol and Hexadecane
• Thermal Conductivity Measurement of Polyglycol Alkyl Ethers at Temperatures from (303.15 to 393.15) K
• Joback Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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