Chemical Properties of 2,5,8,11-Tetraoxadodecane (CAS 112-49-2)

InChI

InChI=1S/C8H18O4/c1-9-3-5-11-7-8-12-6-4-10-2/h3-8H2,1-2H3

InChI Key

YFNKIDBQEZZDLK-UHFFFAOYSA-N

Formula

C8H18O4

SMILES

COCCOCCOCCOC

Molecular Weight¹

178.23

CAS

112-49-2

Other Names

• (CH3O(CH2)2OCH2)2
• 1,2-Bis(methoxyethoxy)ethane
• 1,2-bis(2-methoxyethoxy)ethane
• Ansul Ether 161
• Dimethyl ether of triethylene glycol
• Ethane, 1,2-bis(2-methoxyethoxy)-
• Glyme 4
• Glyme-3
• NSC 66400
• Triethylene glycol dimethyl ether
• methyltriglyme
• triethylene glycol, dimethyl ether
• triglyme
• triglyme (triethylene 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).
• 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_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• IE : Ionization energy (eV).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• 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_boilr : Boiling point at reduced pressure (K).
• T_c : Critical Temperature (K).
• λ : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• V_c : Critical Volume (m³/kmol).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Contents

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

Physical Properties

Property	Value	Unit	Source
ω	0.6146		Relay (1.0) Calculated Property
PAff	946.60	kJ/mol	NIST
BasG	892.40	kJ/mol	NIST
ΔfG°	-403.52	kJ/mol	Joback Calculated Property
ΔfH°gas	-690.18	kJ/mol	Relay (1.0) Calculated Property
ΔfusH°	21.23	kJ/mol	Joback Calculated Property
ΔvapH°	63.70 ± 3.30	kJ/mol	NIST
IE	9.80	eV	NIST
log10WS	0.03		Relay (1.0) Calculated Property
logPoct/wat	0.312		Crippen Calculated Property
McVol	147.060	ml/mol	McGowan Calculated Property
Pc	2370.28	kPa	Joback Calculated Property
Inp	[205.88; 1232.30]
Inp	1232.00		NIST
Inp	1232.30		NIST
Inp	205.88		NIST
Inp	208.42		NIST
Inp	1232.30		NIST
Inp	1232.00		NIST
Inp	205.88		NIST
S°liquid	492.90	J/mol×K	NIST
Tboil	[489.00; 489.20]	K
Tboil	489.20	K	NIST
Tboil	489.00 ± 2.00	K	NIST
Tboil	489.15	K	NIST
Tboil	489.00	K	NIST
Tc	681.20	K	DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development
Tfus	[228.00; 228.15]	K
Tfus	228.15	K	NIST
Tfus	228.00	K	NIST
Ttriple	[229.30; 229.30]	K
Ttriple	229.30 ± 0.20	K	NIST
Ttriple	229.30 ± 0.20	K	NIST
Vc	0.567	m3/kmol	Relay (1.0) Calculated Property

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[359.00; 382.00]	J/mol×K	[298.15; 353.15]
Cp,liquid	367.78	J/mol×K	298.15	NIST
Cp,liquid	368.20	J/mol×K	298.15	NIST
Cp,liquid	359.00	J/mol×K	303.15	Molar Heat Capacity of Aqueous Sulfolane, 4-Formylmorpholine, 1-Methyl-2-pyrrolidinone, and Triethylene Glycol Dimethyl Ether Solutions from (303.15 to 353.15) K
Cp,liquid	364.00	J/mol×K	308.15	Molar Heat Capacity of Aqueous Sulfolane, 4-Formylmorpholine, 1-Methyl-2-pyrrolidinone, and Triethylene Glycol Dimethyl Ether Solutions from (303.15 to 353.15) K
Cp,liquid	366.00	J/mol×K	313.15	Molar Heat Capacity of Aqueous Sulfolane, 4-Formylmorpholine, 1-Methyl-2-pyrrolidinone, and Triethylene Glycol Dimethyl Ether Solutions from (303.15 to 353.15) K
Cp,liquid	368.00	J/mol×K	318.15	Molar Heat Capacity of Aqueous Sulfolane, 4-Formylmorpholine, 1-Methyl-2-pyrrolidinone, and Triethylene Glycol Dimethyl Ether Solutions from (303.15 to 353.15) K
Cp,liquid	370.00	J/mol×K	323.15	Molar Heat Capacity of Aqueous Sulfolane, 4-Formylmorpholine, 1-Methyl-2-pyrrolidinone, and Triethylene Glycol Dimethyl Ether Solutions from (303.15 to 353.15) K
Cp,liquid	371.00	J/mol×K	328.15	Molar Heat Capacity of Aqueous Sulfolane, 4-Formylmorpholine, 1-Methyl-2-pyrrolidinone, and Triethylene Glycol Dimethyl Ether Solutions from (303.15 to 353.15) K
Cp,liquid	373.00	J/mol×K	333.15	Molar Heat Capacity of Aqueous Sulfolane, 4-Formylmorpholine, 1-Methyl-2-pyrrolidinone, and Triethylene Glycol Dimethyl Ether Solutions from (303.15 to 353.15) K
Cp,liquid	375.00	J/mol×K	338.15	Molar Heat Capacity of Aqueous Sulfolane, 4-Formylmorpholine, 1-Methyl-2-pyrrolidinone, and Triethylene Glycol Dimethyl Ether Solutions from (303.15 to 353.15) K
Cp,liquid	379.00	J/mol×K	343.15	Molar Heat Capacity of Aqueous Sulfolane, 4-Formylmorpholine, 1-Methyl-2-pyrrolidinone, and Triethylene Glycol Dimethyl Ether Solutions from (303.15 to 353.15) K
Cp,liquid	381.00	J/mol×K	348.15	Molar Heat Capacity of Aqueous Sulfolane, 4-Formylmorpholine, 1-Methyl-2-pyrrolidinone, and Triethylene Glycol Dimethyl Ether Solutions from (303.15 to 353.15) K
Cp,liquid	382.00	J/mol×K	353.15	Molar Heat Capacity of Aqueous Sulfolane, 4-Formylmorpholine, 1-Methyl-2-pyrrolidinone, and Triethylene Glycol Dimethyl Ether Solutions from (303.15 to 353.15) K
η	[0.0007260; 0.0035600]	Pa×s	[273.15; 363.15]
η	0.0035600	Pa×s	273.15	Density, viscosity and solubility of carbon dioxide in glymes
η	0.0031000	Pa×s	278.15	Density, viscosity and solubility of carbon dioxide in glymes
η	0.0027500	Pa×s	283.15	Density, viscosity and solubility of carbon dioxide in glymes
η	0.0024500	Pa×s	288.15	Density, viscosity and solubility of carbon dioxide in glymes
η	0.0021900	Pa×s	293.15	Density, viscosity and solubility of carbon dioxide in glymes
η	0.0019600	Pa×s	298.15	Density, viscosity and solubility of carbon dioxide in glymes
η	0.0017700	Pa×s	303.15	Densities, Viscosities and Derived Functions of Binary Mixtures: (Triethylene Glycol Dimethyl Ether + Water) and (N-acetylmorpholine+ Water) from 298.15 to 343.15 K
η	0.0017800	Pa×s	303.15	Density, viscosity and solubility of carbon dioxide in glymes
η	0.0014800	Pa×s	313.15	Density, viscosity and solubility of carbon dioxide in glymes
η	0.0014800	Pa×s	313.15	Densities, Viscosities and Derived Functions of Binary Mixtures: (Triethylene Glycol Dimethyl Ether + Water) and (N-acetylmorpholine+ Water) from 298.15 to 343.15 K
η	0.0012500	Pa×s	323.15	Density, viscosity and solubility of carbon dioxide in glymes
η	0.0012600	Pa×s	323.15	Densities, Viscosities and Derived Functions of Binary Mixtures: (Triethylene Glycol Dimethyl Ether + Water) and (N-acetylmorpholine+ Water) from 298.15 to 343.15 K
η	0.0010800	Pa×s	333.15	Density, viscosity and solubility of carbon dioxide in glymes
η	0.0010800	Pa×s	333.15	Densities, Viscosities and Derived Functions of Binary Mixtures: (Triethylene Glycol Dimethyl Ether + Water) and (N-acetylmorpholine+ Water) from 298.15 to 343.15 K
η	0.0009360	Pa×s	343.15	Density, viscosity and solubility of carbon dioxide in glymes
η	0.0009450	Pa×s	343.15	Densities, Viscosities and Derived Functions of Binary Mixtures: (Triethylene Glycol Dimethyl Ether + Water) and (N-acetylmorpholine+ Water) from 298.15 to 343.15 K
η	0.0008210	Pa×s	353.15	Density, viscosity and solubility of carbon dioxide in glymes
η	0.0007260	Pa×s	363.15	Density, viscosity and solubility of carbon dioxide in glymes
εr	[6.90; 7.89]		[288.15; 328.15]
εr	7.88		288.15	On permittivity and density of the systems {triglyme + (dimethyl or diethyl carbonate)} and formulation of De in terms of volume or mole fraction
εr	7.89		288.15	Permittivity and density of the systems (monoglyme, diglyme, triglyme, or tetraglyme + n-heptane) at several temperatures
εr	7.58		298.15	On permittivity and density of the systems {triglyme + (dimethyl or diethyl carbonate)} and formulation of De in terms of volume or mole fraction
εr	7.63		298.15	Permittivity and density of the systems (monoglyme, diglyme, triglyme, or tetraglyme + n-heptane) at several temperatures
εr	7.33		308.15	On permittivity and density of the systems {triglyme + (dimethyl or diethyl carbonate)} and formulation of De in terms of volume or mole fraction
εr	7.38		308.15	Permittivity and density of the systems (monoglyme, diglyme, triglyme, or tetraglyme + n-heptane) at several temperatures
εr	7.09		318.15	On permittivity and density of the systems {triglyme + (dimethyl or diethyl carbonate)} and formulation of De in terms of volume or mole fraction
εr	6.90		328.15	On permittivity and density of the systems {triglyme + (dimethyl or diethyl carbonate)} and formulation of De in terms of volume or mole fraction
ΔfusH	[23.71; 23.71]	kJ/mol	[229.30; 229.30]
ΔfusH	23.71	kJ/mol	229.30	NIST
ΔfusH	23.71	kJ/mol	229.30	NIST
ΔfusH	23.71	kJ/mol	229.30	NIST
ΔfusH	23.71	kJ/mol	229.30	NIST
n0	[1.41250; 1.42500]		[288.15; 318.15]
n0	1.42500		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	1.42090		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	1.41670		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	1.41250		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	[909.70; 994.10]	kg/m3	[283.15; 373.15]
ρl	994.10	kg/m3	283.15	Thermophysical properties of glycols and glymes
ρl	990.80	kg/m3	288.15	Thermophysical properties of glycols and glymes
ρl	989.40	kg/m3	288.15	Thermophysical properties of glycols and glymes
ρl	989.16	kg/m3	288.15	On the permittivity and density measurements of binary systems of {triglyme + (n-nonane or n-dodecane) } at various temperatures
ρl	984.16	kg/m3	293.15	On the permittivity and density measurements of binary systems of {triglyme + (n-nonane or n-dodecane) } at various temperatures
ρl	984.60	kg/m3	293.15	Thermophysical properties of glycols and glymes
ρl	986.00	kg/m3	293.15	Thermophysical properties of glycols and glymes
ρl	981.50	kg/m3	298.15	Thermophysical properties of glycols and glymes
ρl	980.42	kg/m3	298.15	Liquid-Liquid Equilibrium of Ternary Mixtures Formed by Some Oligooxaethylenes with Ethanol and Hexadecane
ρl	979.61	kg/m3	298.15	On the permittivity and density measurements of binary systems of {triglyme + (n-nonane or n-dodecane) } at various temperatures
ρl	979.90	kg/m3	298.15	Thermophysical properties of glycols and glymes
ρl	980.62	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	975.10	kg/m3	303.15	Thermophysical properties of glycols and glymes
ρl	976.70	kg/m3	303.15	Thermophysical properties of glycols and glymes
ρl	974.85	kg/m3	303.15	On the permittivity and density measurements of binary systems of {triglyme + (n-nonane or n-dodecane) } at various temperatures
ρl	971.90	kg/m3	308.15	Thermophysical properties of glycols and glymes
ρl	970.40	kg/m3	308.15	Thermophysical properties of glycols and glymes
ρl	970.85	kg/m3	308.15	On the permittivity and density measurements of binary systems of {triglyme + (n-nonane or n-dodecane) } at various temperatures
ρl	967.20	kg/m3	313.15	Thermophysical properties of glycols and glymes
ρl	965.60	kg/m3	313.15	Thermophysical properties of glycols and glymes
ρl	962.40	kg/m3	318.15	Thermophysical properties of glycols and glymes
ρl	960.67	kg/m3	318.15	On the permittivity and density measurements of binary systems of {triglyme + (n-nonane or n-dodecane) } at various temperatures
ρl	957.70	kg/m3	323.15	Thermophysical properties of glycols and glymes
ρl	956.10	kg/m3	323.15	Thermophysical properties of glycols and glymes
ρl	952.90	kg/m3	328.15	Thermophysical properties of glycols and glymes
ρl	951.06	kg/m3	328.15	On the permittivity and density measurements of binary systems of {triglyme + (n-nonane or n-dodecane) } at various temperatures
ρl	946.50	kg/m3	333.15	Thermophysical properties of glycols and glymes
ρl	948.10	kg/m3	333.15	Thermophysical properties of glycols and glymes
ρl	943.30	kg/m3	338.15	Thermophysical properties of glycols and glymes
ρl	938.60	kg/m3	343.15	Thermophysical properties of glycols and glymes
ρl	936.90	kg/m3	343.15	Thermophysical properties of glycols and glymes
ρl	933.80	kg/m3	348.15	Thermophysical properties of glycols and glymes
ρl	929.00	kg/m3	353.15	Thermophysical properties of glycols and glymes
ρl	924.20	kg/m3	358.15	Thermophysical properties of glycols and glymes
ρl	919.40	kg/m3	363.15	Thermophysical properties of glycols and glymes
ρl	914.50	kg/m3	368.15	Thermophysical properties of glycols and glymes
ρl	909.70	kg/m3	373.15	Thermophysical properties of glycols and glymes
ΔfusS	[103.40; 103.40]	J/mol×K	[229.30; 229.30]
ΔfusS	103.40	J/mol×K	229.30	NIST
ΔfusS	103.40	J/mol×K	229.30	NIST
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	[0.12; 0.14]	W/m×K	[302.75; 392.16]
λ	0.14	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	0.12	W/m×K	392.16	Thermal Conductivity Measurement of Polyglycol Alkyl Ethers at Temperatures from (303.15 to 393.15) K

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboilr	[376.60; 376.70]	K	[1.30; 1.30]
Tboilr	376.70	K	1.30	NIST
Tboilr	376.60	K	1.30	NIST

Datasets

1. Viscosity, Pa*s (1)
2. Speed of sound, m/s (1)

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
293.15	100.00	0.0021
293.15	20000.00	0.0025
293.15	40000.00	0.0030
293.15	60000.00	0.0034
293.15	80000.00	0.0039
293.15	100000.00	0.0044
313.15	100.00	0.0015
313.15	20000.00	0.0018
313.15	40000.00	0.0020
313.15	60000.00	0.0024
313.15	80000.00	0.0027
313.15	100000.00	0.0030
333.15	100.00	0.0011
333.15	20000.00	0.0013
333.15	40000.00	0.0015
333.15	60000.00	0.0017
333.15	80000.00	0.0019
333.15	100000.00	0.0021
353.15	100.00	0.0008
353.15	20000.00	0.0010
353.15	40000.00	0.0011
353.15	60000.00	0.0013
353.15	80000.00	0.0015
353.15	100000.00	0.0016
Reference

Speed of sound, m/s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Speed of sound, m/s - Liquid
293.15	100.00	1361.9
293.15	10000.00	1403.1
293.15	20000.00	1442.5
293.15	30000.00	1479.3
293.15	40000.00	1514.7
293.15	50000.00	1547.8
293.15	60000.00	1579.5
293.15	70000.00	1610.0
293.15	80000.00	1639.3
293.15	90000.00	1667.4
293.15	100000.00	1694.6
303.15	100.00	1323.2
303.15	10000.00	1366.5
303.15	20000.00	1407.2
303.15	30000.00	1445.2
303.15	40000.00	1481.6
303.15	50000.00	1515.7
303.15	60000.00	1548.2
303.15	70000.00	1579.4
303.15	80000.00	1609.3
303.15	90000.00	1638.2
303.15	100000.00	1665.9
313.15	100.00	1285.1
313.15	10000.00	1330.0
313.15	20000.00	1372.2
313.15	30000.00	1411.8
313.15	40000.00	1448.8
313.15	50000.00	1484.1
313.15	60000.00	1517.5
313.15	70000.00	1549.7
313.15	80000.00	1580.3
313.15	90000.00	1609.9
313.15	100000.00	1638.1
323.15	100.00	1247.7
323.15	10000.00	1294.6
323.15	20000.00	1338.5
323.15	30000.00	1379.1
323.15	40000.00	1417.3
323.15	50000.00	1453.6
323.15	60000.00	1487.9
323.15	70000.00	1520.7
323.15	80000.00	1552.0
323.15	90000.00	1581.9
323.15	100000.00	1610.8
333.15	100.00	1210.9
333.15	10000.00	1259.5
333.15	20000.00	1304.8
333.15	30000.00	1346.9
333.15	40000.00	1386.3
333.15	50000.00	1423.4
333.15	60000.00	1458.8
333.15	70000.00	1492.1
333.15	80000.00	1524.3
333.15	90000.00	1554.8
333.15	100000.00	1584.3
343.15	100.00	1174.6
343.15	10000.00	1225.1
343.15	20000.00	1272.0
343.15	30000.00	1315.6
343.15	40000.00	1356.2
343.15	50000.00	1394.1
343.15	60000.00	1430.3
343.15	70000.00	1464.6
343.15	80000.00	1497.2
343.15	90000.00	1528.4
343.15	100000.00	1558.5
353.15	100.00	1138.7
353.15	10000.00	1191.5
353.15	20000.00	1240.0
353.15	30000.00	1284.6
353.15	40000.00	1326.2
353.15	50000.00	1365.6
353.15	60000.00	1402.4
353.15	70000.00	1437.6
353.15	80000.00	1470.9
353.15	90000.00	1502.6
353.15	100000.00	1533.4
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[236.81; 506.06]	J/mol×K	[273.00; 1000.00]	Joback Predicted correlation
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K
Coefficient A			9.76160e+01
Coefficient B			5.11040e-01
Coefficient C			3.26000e-05
Coefficient D			-1.35200e-07
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	236.81	J/mol×K	273.00	Calculated Property
Cp,gas	276.50	J/mol×K	353.78	Calculated Property
Cp,gas	314.75	J/mol×K	434.56	Calculated Property
Cp,gas	351.13	J/mol×K	515.33	Calculated Property
Cp,gas	385.20	J/mol×K	596.11	Calculated Property
Cp,gas	416.54	J/mol×K	676.89	Calculated Property
Cp,gas	444.72	J/mol×K	757.67	Calculated Property
Cp,gas	469.32	J/mol×K	838.44	Calculated Property
Cp,gas	489.91	J/mol×K	919.22	Calculated Property
Cp,gas	506.06	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.66]	kPa	[372.99; 516.68]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.57644e+01
Coefficient B			-4.62697e+03
Coefficient C			-7.40300e+01
Temperature range, min.			372.99
Temperature range, max.			516.68
Pvap	1.33	kPa	372.99	Calculated Property
Pvap	2.92	kPa	388.96	Calculated Property
Pvap	5.94	kPa	404.92	Calculated Property
Pvap	11.30	kPa	420.89	Calculated Property
Pvap	20.32	kPa	436.85	Calculated Property
Pvap	34.79	kPa	452.82	Calculated Property
Pvap	57.01	kPa	468.78	Calculated Property
Pvap	89.92	kPa	484.75	Calculated Property
Pvap	137.06	kPa	500.71	Calculated Property
Pvap	202.66	kPa	516.68	Calculated Property

Similar Compounds

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

Mixtures

• Ethane, fluoro- + 2,5,8,11-Tetraoxadodecane
• 2,5,8,11-Tetraoxadodecane + Carbonic acid, dimethyl ester
• Diethyl carbonate + 2,5,8,11-Tetraoxadodecane
• 2,5,8,11-Tetraoxadodecane + Heptane
• 2,5,8,11-Tetraoxadodecane + Nonane
• 2,5,8,11-Tetraoxadodecane + Dodecane
• 2,5,8,11-Tetraoxadodecane + Norflurane
• 2,5,8,11-Tetraoxadodecane + Carbon dioxide
• 2,5,8,11-Tetraoxadodecane + Water
• 2,5,8,11-Tetraoxadodecane + Ethane, 1,1-difluoro-
• 2,5,8,11-Tetraoxadodecane + Ethanol
• helium + 2,5,8,11-Tetraoxadodecane
• 2,5,8,11-Tetraoxadodecane + neon
• 2,5,8,11-Tetraoxadodecane + Argon
• 2,5,8,11-Tetraoxadodecane + Krypton
• Xenon + 2,5,8,11-Tetraoxadodecane
• Hydrogen + 2,5,8,11-Tetraoxadodecane
• Nitrogen + 2,5,8,11-Tetraoxadodecane
• 2,5,8,11-Tetraoxadodecane + Methane
• 2,5,8,11-Tetraoxadodecane + Ethylene

Find more mixtures with 2,5,8,11-Tetraoxadodecane.

Sources

• Cheméo Relay (1.0)
• Crippen Method
• Crippen Method
• High-pressure viscosity behavior of x 1,1,1,2-tetrafluoroethane (HFC-134a) + (1-x) triethylene glycol dimethylether (TriEGDME) mixtures: Measurements and modeling
• Density, viscosity and solubility of carbon dioxide in glymes
• On the permittivity and density measurements of binary systems of {triglyme + (n-nonane or n-dodecane) } at various temperatures
• Bubble pressure measurements for the (1,1,1,2-tetrafluoroethane + triethylene glycol dimethyl ether) system
• On permittivity and density of the systems {triglyme + (dimethyl or diethyl carbonate)} and 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
• 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
• Measurement and Correlation of Isothermal Vapor Liquid Equilibrium of Fluoroethane + Dimethyl Ether Triethylene Glycol, 1,1-Difluoroethane + Dimethyl Ether Triethylene Glycol, and 1,1-Difluoroethane + N-Methyl-2-pyrrolidone Systems
• 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
• Isothermal Vapor-Liquid Equilibria of the Absorption Working Pairs (R1234yf + NMP, R1234yf + DMETrEG) at Temperatures from 293.15 K to 353.15 K
• DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development
• Isothermal Vapor-Liquid Equilibrium of the Absorption Working Pairs (HFC-32 + DMETrEG, HFC-32 + NMP) at Temperatures from 293.15 to 343.15 K
• 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
• 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
• Densities, Viscosities and Derived Functions of Binary Mixtures: (Triethylene Glycol Dimethyl Ether + Water) and (N-acetylmorpholine+ Water) from 298.15 to 343.15 K
• Solubility Study of Methane and Ethane In Promising Physical Solvents for Natural Gas Sweetening Operations
• P-rho-T-x Measurements for (1,1,1,2-Tetrafluoroethane + Triethylene Glycol Dimethyl Ether) at High Haloalkane Content
• 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
• 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
• Molar Heat Capacity of Aqueous Sulfolane, 4-Formylmorpholine, 1-Methyl-2-pyrrolidinone, and Triethylene Glycol Dimethyl Ether Solutions from (303.15 to 353.15) 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)
• Joback Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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