Chemical Properties of Tetraglyme (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

• 2,5,8,11,14-Pentaoxapentadecane
• Ansul Ether 181AT
• Bis[2-(2-methoxyethoxy)ethyl] ether
• CH3O[CH2CH2O]4CH3
• Dimethoxytetraethylene glycol
• Dimethoxytetraglycol
• 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
• tetraethylene glycol, dimethyl ether

• 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).
• η : Dynamic viscosity (Pa×s).
• 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_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 : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• V_c : Critical Volume (m³/kmol).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Contents

1. Physical Properties
2. Temperature Dependent Properties
3. Datasets
4. Correlations
5. Similar Compounds
6. Mixtures
7. Sources

Physical Properties

Property	Value	Unit	Source
ω	0.7212		Relay (1.0) Calculated Property
PAff	953.80	kJ/mol	NIST
BasG	897.80	kJ/mol	NIST
ΔfG°	-491.68	kJ/mol	Joback Calculated Property
ΔfH°gas	-855.35	kJ/mol	Relay (1.0) Calculated Property
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	1952.68	kPa	Joback Calculated Property
Tboil	[548.15; 549.00]	K
Tboil	549.00	K	NIST
Tboil	548.15	K	NIST
Tc	694.20	K	Relay (1.0) Calculated Property
Tfus	243.45	K	NIST
Vc	0.700	m3/kmol	Relay (1.0) Calculated Property

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[449.87; 529.06]	J/mol×K	[540.30; 702.78]
Cp,gas	449.87	J/mol×K	540.30	Joback Calculated Property
Cp,gas	464.04	J/mol×K	567.38	Joback Calculated Property
Cp,gas	477.85	J/mol×K	594.46	Joback Calculated Property
Cp,gas	491.28	J/mol×K	621.54	Joback Calculated Property
Cp,gas	504.30	J/mol×K	648.62	Joback Calculated Property
Cp,gas	516.90	J/mol×K	675.70	Joback Calculated Property
Cp,gas	529.06	J/mol×K	702.78	Joback Calculated Property
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
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	1.43030		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	1.42620		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	1020.30	kg/m3	283.15	The Viscosity and Density of Ionic Liquid + Tetraglyme Mixtures and the Effect of Tetraglyme on CO2 Solubility
ρl	1020.70	kg/m3	283.15	Thermophysical properties of glycols and glymes
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	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	1015.63	kg/m3	288.15	Volumetric and viscometric properties of binary liquid mixtures as potential solvents for flue gas desulfurization processes
ρl	1017.00	kg/m3	288.15	Thermophysical properties of glycols and glymes
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	1015.60	kg/m3	288.15	The Viscosity and Density of Ionic Liquid + Tetraglyme Mixtures and the Effect of Tetraglyme on CO2 Solubility
ρl	1016.10	kg/m3	288.15	Thermophysical properties of glycols and glymes
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	1011.50	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 Behavior of Binary Systems 2-Butanol + PEG 200, + PEG 400, + Tetraethylene Glycol Dimethyl Ether, and + N-Methyl-2-pyrrolidone
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	1012.30	kg/m3	293.15	Thermophysical properties of glycols and glymes
ρl	1011.00	kg/m3	293.15	Volumetric and viscometric properties of binary liquid mixtures as potential solvents for flue gas desulfurization processes
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	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 Behavior of Binary Systems 2-Butanol + PEG 200, + PEG 400, + Tetraethylene Glycol Dimethyl Ether, and + N-Methyl-2-pyrrolidone
ρl	1006.20	kg/m3	298.15	Liquid-Liquid Equilibrium of Ternary Mixtures Formed by Some Oligooxaethylenes with Ethanol and Hexadecane
ρl	1006.36	kg/m3	298.15	Volumetric and viscometric properties of binary liquid mixtures as potential solvents for flue gas desulfurization processes
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	1007.60	kg/m3	298.15	Thermophysical properties of glycols and glymes
ρl	1006.80	kg/m3	298.15	Thermophysical properties of glycols and glymes
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	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	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 and Viscometric Behavior of Binary Systems 2-Butanol + PEG 200, + PEG 400, + Tetraethylene Glycol Dimethyl Ether, and + N-Methyl-2-pyrrolidone
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	1002.20	kg/m3	303.15	Thermophysical properties of glycols and glymes
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	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	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	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 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	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	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	992.48	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	994.10	kg/m3	313.15	Thermophysical properties of glycols and glymes
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	992.48	kg/m3	313.15	Volumetric and viscometric properties of binary liquid mixtures as potential solvents for flue gas desulfurization processes
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	989.50	kg/m3	318.15	Thermophysical properties of glycols and glymes
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	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	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	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	983.70	kg/m3	323.15	Thermophysical properties of glycols and glymes
ρl	983.23	kg/m3	323.15	Volumetric and viscometric properties of binary liquid mixtures as potential solvents for flue gas desulfurization processes
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	984.90	kg/m3	323.15	Thermophysical properties of glycols and glymes
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	983.40	kg/m3	323.15	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	978.80	kg/m3	328.15	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 Properties, Viscosities, and Refractive Indices of the Binary Systems 1-Butanol + PEG 200, + PEG 400, and + TEGDME
ρl	974.50	kg/m3	333.15	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	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	965.00	kg/m3	343.15	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	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
λ	[0.13; 0.15]	W/m×K	[302.75; 392.16]
λ	0.15	W/m×K	302.75	Thermal Conductivity Measurement of Polyglycol Alkyl Ethers at Temperatures from (303.15 to 393.15) K
λ	0.14	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	0.13	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
Pvap	[1.33; 202.64]	kPa	[419.76; 578.51]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
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

Similar Compounds

Find more compounds similar to Tetraglyme.

Mixtures

• Tetraglyme + 1-Butanol
• Carbon dioxide + Tetraglyme
• Tetraglyme + Propanoic acid, 2-hydroxy-, ethyl ester
• Tetraglyme + Heptane
• Tetraglyme + Octane
• Ethanol + Tetraglyme
• Tetraglyme + Water
• Tetraglyme + Tetradecane
• Hexadecane + Ethanol + Tetraglyme
• Tetraglyme + Norflurane
• 1,2-Ethanediol + Tetraglyme + Sulfur dioxide
• helium + Tetraglyme
• neon + Tetraglyme
• Tetraglyme + Argon
• Tetraglyme + Krypton
• Xenon + Tetraglyme
• Hydrogen + Tetraglyme
• Nitrogen + Tetraglyme
• Methane + Tetraglyme
• Tetraglyme + Ethylene

Find more mixtures with Tetraglyme.

Sources

• Cheméo Relay (1.0)
• 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
• Volumetric and viscometric properties of binary liquid mixtures as potential solvents for flue gas desulfurization processes
• Thermophysical properties of glycols and glymes
• The Viscosity and Density of Ionic Liquid + Tetraglyme Mixtures and the Effect of Tetraglyme on CO2 Solubility
• 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
• 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
• 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

Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more. Take the time to validate and double check the source of the data.