Chemical Properties of Propane, 2-methoxy-2-methyl- (CAS 1634-04-4)

InChI

InChI=1S/C5H12O/c1-5(2,3)6-4/h1-4H3

InChI Key

BZLVMXJERCGZMT-UHFFFAOYSA-N

Formula

C5H12O

SMILES

COC(C)(C)C

Molecular Weight¹

88.15

CAS

1634-04-4

Other Names

• 1,1-dimethyl-1-methoxyethane
• 1,1-dimethylethyl methyl ether
• 2-Methyl-2-methoxypropane
• 2-methoxy-2-methylpropane
• 3,3-dimethyl-2-oxabutane
• Driveron
• Ether, tert-butyl methyl
• METHYL-1,1-DIMETHYLETHYL ETHER
• MTBE
• Methyl t-butyl ether
• UN 2398
• methyl 1,1-dimethylethyl ether
• methyl tert-butyl ether
• methyl tert-butyl ether (MTBE)
• t-Butyl methyl ether
• tert-C4H9OCH3
• tert-butyl methyl ether

• 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).
• C_sat : Molar heat capacity at saturation pressure (J/mol×K).
• μ : Dipole Moment (debye).
• 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_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).
• ν : Kinematic viscosity (m²/s).
• 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).
• I_np : Non-polar retention indices.
• I_p : Polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_gas : Molar entropy at standard conditions (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).
• α_diff : Thermal diffusivity (m²/s).
• 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.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	[0.2661; 0.2690]
ω	0.2670		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.2661		ChemSep v8.3 pure component data Compiled value
ω	0.2690		KDB
PAff	841.60	kJ/mol	NIST
BasG	812.40	kJ/mol	NIST
ΔcH°liquid	[-3368.97; -3359.70]	kJ/mol
ΔcH°liquid	-3368.97	kJ/mol	NIST
ΔcH°liquid	-3359.70 ± 6.50	kJ/mol	NIST
μ	[1.20; 1.36]	debye
μ	1.36	debye	ChemSep v8.3 pure component data Compiled value
μ	1.20	debye	KDB
η	0.0003610	Pa×s	Densities and Viscosities for the Ternary Systems of Methyl tert-Butyl Ether + Methanol + Benzene and Methyl tert-Butyl Ether + Methanol + Toluene and Their Sub-binary Systems at 298.15 K
ΔfG°	[-125.50; -117.50]	kJ/mol
ΔfG°	-117.50	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	-125.50	kJ/mol	KDB
ΔfH°gas	[-293.10; -282.20]	kJ/mol
ΔfH°gas	-283.50	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-293.10	kJ/mol	KDB
ΔfH°gas	-285.00	kJ/mol	NIST
ΔfH°gas	-283.20 ± 1.30	kJ/mol	NIST
ΔfH°gas	-282.20 ± 1.90	kJ/mol	NIST
ΔfH°liquid	[-322.90; -313.60]	kJ/mol
ΔfH°liquid	-315.40	kJ/mol	NIST
ΔfH°liquid	-313.60 ± 1.30	kJ/mol	NIST
ΔfH°liquid	-322.90 ± 5.00	kJ/mol	NIST
ΔfusH°	2.48	kJ/mol	Joback Calculated Property
ΔvapH°	[29.60; 30.40]	kJ/mol
ΔvapH°	30.04	kJ/mol	NIST
ΔvapH°	29.81	kJ/mol	NIST
ΔvapH°	29.80	kJ/mol	NIST
ΔvapH°	29.60	kJ/mol	NIST
ΔvapH°	30.39 ± 0.09	kJ/mol	NIST
ΔvapH°	30.40 ± 0.10	kJ/mol	NIST
ΔvapH°	30.00	kJ/mol	NIST
IE	[9.24; 9.48]	eV
IE	9.24	eV	NIST
IE	9.48	eV	NIST
IE	9.41	eV	NIST
log10WS	[-0.24; -0.24]
log10WS	-0.24		Aq. Solubility Prediction
log10WS	-0.24		Estimated Solubility
logPoct/wat	1.240		NCMS SOLV-DB
McVol	87.180	ml/mol	McGowan Calculated Property
Pc	[3397.00; 3434.92]	kPa
Pc	3430.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Pc	3434.92	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	3430.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	3430.00	kPa	KDB
Pc	Outlier 3397.00 ± 8.00	kPa	NIST
Pc	3430.00 ± 10.00	kPa	NIST
Ptriple	5.36e-04	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[544.00; 570.12]
Inp	563.70		NIST
Inp	563.70		NIST
Inp	562.70		NIST
Inp	562.00		NIST
Inp	Outlier 544.00		NIST
Inp	549.00		NIST
Inp	570.12		NIST
Inp	568.00		NIST
Inp	566.00		NIST
Inp	566.00		NIST
Inp	567.00		NIST
Inp	554.50		NIST
Inp	558.00		NIST
Inp	563.00		NIST
Inp	570.00		NIST
Inp	560.00		NIST
Inp	556.00		NIST
Inp	556.00		NIST
Inp	556.00		NIST
Inp	560.00		NIST
Inp	568.00		NIST
Inp	563.00		NIST
Inp	556.00		NIST
Ip	[666.00; 688.00]
Ip	666.00		NIST
Ip	688.00		NIST
S°gas	357.80	J/mol×K	NIST
S°liquid	265.30	J/mol×K	NIST
Tboil	[328.00; 328.40]	K
Tboil	328.25	K	Vapor-Liquid Equilibria for the Binary Systems of Dimethoxymethane with Some Fuel Oxygenates
Tboil	328.35	K	ChemSep v8.3 pure component data Compiled value
Tboil	328.30	K	KDB
Tboil	328.35	K	NCMS SOLV-DB
Tboil	328.20 ± 0.30	K	NIST
Tboil	328.20 ± 0.30	K	NIST
Tboil	328.11 ± 0.30	K	NIST
Tboil	328.40	K	NIST
Tboil	Outlier 328.00	K	NIST
Tboil	328.30	K	NIST
Tboil	328.21 ± 0.10	K	NIST
Tboil	328.30 ± 0.40	K	NIST
Tboil	328.40 ± 0.30	K	NIST
Tc	[496.40; 497.10]	K
Tc	497.00	K	Measurement of critical temperatures and critical pressures for binary mixtures of methyl tert-butyl ether (MTBE) + alcohol and MTBE + alkane
Tc	497.10	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Tc	497.10	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	497.10	K	ChemSep v8.3 pure component data Compiled value
Tc	497.10	K	KDB
Tc	Outlier 496.40 ± 0.30	K	NIST
Tc	497.10	K	NIST
Tc	497.10 ± 0.20	K	NIST
Tfus	[164.15; 164.55]	K
Tfus	164.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	164.55	K	ChemSep v8.3 pure component data Compiled value
Tfus	164.50	K	KDB
Tfus	164.25	K	Aq. Solubility Prediction
Tfus	164.15	K	NCMS SOLV-DB
Tfus	164.50 ± 0.20	K	NIST
Ttriple	[164.55; 164.56]	K
Ttriple	164.55	K	ChemSep v8.3 pure component data Compiled value
Ttriple	164.56 ± 0.07	K	NIST
Ttriple	164.56 ± 0.07	K	NIST
UQi	3.63		ChemSep v8.3 pure component data Compiled value
URi	4.07		ChemSep v8.3 pure component data Compiled value
Vc	[0.319; 0.329]	m3/kmol
Vc	0.319	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.329	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.323	m3/kmol	KDB
Zc	[0.2676350; 0.2730000]
Zc	0.2730000		ChemSep v8.3 pure component data Compiled value
Zc	0.2676350		KDB
Zra	0.27		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[187.50; 188.00]	J/mol×K	[298.00; 298.15]
Cp,liquid	188.00	J/mol×K	298.00	NIST
Cp,liquid	187.50	J/mol×K	298.15	NIST
Cp,liquid	187.80	J/mol×K	298.15	NIST
Csat	[180.90; 198.00]	J/mol×K	[277.15; 325.15]
Csat	180.90	J/mol×K	277.15	Oxygenated Gasoline Additives: Saturated Heat Capacities between (277 and 355) K
Csat	181.40	J/mol×K	279.15	Oxygenated Gasoline Additives: Saturated Heat Capacities between (277 and 355) K
Csat	182.30	J/mol×K	281.16	Oxygenated Gasoline Additives: Saturated Heat Capacities between (277 and 355) K
Csat	183.10	J/mol×K	283.15	Oxygenated Gasoline Additives: Saturated Heat Capacities between (277 and 355) K
Csat	183.80	J/mol×K	285.15	Oxygenated Gasoline Additives: Saturated Heat Capacities between (277 and 355) K
Csat	184.40	J/mol×K	287.14	Oxygenated Gasoline Additives: Saturated Heat Capacities between (277 and 355) K
Csat	185.30	J/mol×K	289.16	Oxygenated Gasoline Additives: Saturated Heat Capacities between (277 and 355) K
Csat	186.00	J/mol×K	291.15	Oxygenated Gasoline Additives: Saturated Heat Capacities between (277 and 355) K
Csat	186.80	J/mol×K	293.16	Oxygenated Gasoline Additives: Saturated Heat Capacities between (277 and 355) K
Csat	187.70	J/mol×K	295.15	Oxygenated Gasoline Additives: Saturated Heat Capacities between (277 and 355) K
Csat	188.30	J/mol×K	297.14	Oxygenated Gasoline Additives: Saturated Heat Capacities between (277 and 355) K
Csat	189.00	J/mol×K	299.14	Oxygenated Gasoline Additives: Saturated Heat Capacities between (277 and 355) K
Csat	189.70	J/mol×K	301.16	Oxygenated Gasoline Additives: Saturated Heat Capacities between (277 and 355) K
Csat	190.40	J/mol×K	303.16	Oxygenated Gasoline Additives: Saturated Heat Capacities between (277 and 355) K
Csat	191.10	J/mol×K	305.15	Oxygenated Gasoline Additives: Saturated Heat Capacities between (277 and 355) K
Csat	191.80	J/mol×K	307.15	Oxygenated Gasoline Additives: Saturated Heat Capacities between (277 and 355) K
Csat	192.60	J/mol×K	309.16	Oxygenated Gasoline Additives: Saturated Heat Capacities between (277 and 355) K
Csat	193.20	J/mol×K	311.16	Oxygenated Gasoline Additives: Saturated Heat Capacities between (277 and 355) K
Csat	193.90	J/mol×K	313.15	Oxygenated Gasoline Additives: Saturated Heat Capacities between (277 and 355) K
Csat	194.60	J/mol×K	315.15	Oxygenated Gasoline Additives: Saturated Heat Capacities between (277 and 355) K
Csat	195.20	J/mol×K	317.14	Oxygenated Gasoline Additives: Saturated Heat Capacities between (277 and 355) K
Csat	196.00	J/mol×K	319.16	Oxygenated Gasoline Additives: Saturated Heat Capacities between (277 and 355) K
Csat	196.50	J/mol×K	321.15	Oxygenated Gasoline Additives: Saturated Heat Capacities between (277 and 355) K
Csat	197.30	J/mol×K	323.15	Oxygenated Gasoline Additives: Saturated Heat Capacities between (277 and 355) K
Csat	198.00	J/mol×K	325.15	Oxygenated Gasoline Additives: Saturated Heat Capacities between (277 and 355) K
η	[0.0002780; 0.0004430]	Pa×s	[273.15; 313.15]
η	0.0004430	Pa×s	273.15	Densities and Viscosities of MTBE + Heptane or Octane at p ) 0.1 MPa from (273.15 to 363.15) K
η	0.0003900	Pa×s	273.15	Density, Viscosity, Vapor-Liquid Equilibrium, and Excess Molar Enthalpy of [Chloroform + Methyl tert-Butyl Ether]
η	0.0004170	Pa×s	278.15	Densities and Viscosities of MTBE + Heptane or Octane at p ) 0.1 MPa from (273.15 to 363.15) K
η	0.0003600	Pa×s	283.15	Density, Viscosity, Vapor-Liquid Equilibrium, and Excess Molar Enthalpy of [Chloroform + Methyl tert-Butyl Ether]
η	0.0003920	Pa×s	283.15	Densities and Viscosities of MTBE + Heptane or Octane at p ) 0.1 MPa from (273.15 to 363.15) K
η	0.0003897	Pa×s	283.15	Experimental and Predicted Viscosities of Binary Mixtures Containing Chlorinated and Oxygenated Compounds
η	0.0003640	Pa×s	288.15	Experimental and Predicted Viscosities of Binary Mixtures Containing Chlorinated and Oxygenated Compounds
η	0.0003700	Pa×s	288.15	Densities and Viscosities of MTBE + Heptane or Octane at p ) 0.1 MPa from (273.15 to 363.15) K
η	0.0003330	Pa×s	293.15	Density, Viscosity, Vapor-Liquid Equilibrium, and Excess Molar Enthalpy of [Chloroform + Methyl tert-Butyl Ether]
η	0.0003482	Pa×s	293.15	Experimental and Predicted Viscosities of Binary Mixtures Containing Chlorinated and Oxygenated Compounds
η	0.0003400	Pa×s	298.15	NCMS SOLV-DB
η	0.0003190	Pa×s	298.15	Density, Viscosity, Vapor-Liquid Equilibrium, and Excess Molar Enthalpy of [Chloroform + Methyl tert-Butyl Ether]
η	0.0003327	Pa×s	298.15	Experimental and Predicted Viscosities of Binary Mixtures Containing Chlorinated and Oxygenated Compounds
η	0.0003152	Pa×s	303.15	Experimental and Predicted Viscosities of Binary Mixtures Containing Chlorinated and Oxygenated Compounds
η	0.0003040	Pa×s	303.15	Density, Viscosity, Vapor-Liquid Equilibrium, and Excess Molar Enthalpy of [Chloroform + Methyl tert-Butyl Ether]
η	0.0002994	Pa×s	308.15	Experimental and Predicted Viscosities of Binary Mixtures Containing Chlorinated and Oxygenated Compounds
η	0.0002780	Pa×s	313.15	Density, Viscosity, Vapor-Liquid Equilibrium, and Excess Molar Enthalpy of [Chloroform + Methyl tert-Butyl Ether]
η	0.0002846	Pa×s	313.15	Experimental and Predicted Viscosities of Binary Mixtures Containing Chlorinated and Oxygenated Compounds
ΔfusH	[7.60; 7.60]	kJ/mol	[164.56; 164.60]
ΔfusH	7.60	kJ/mol	164.56	NIST
ΔfusH	7.60	kJ/mol	164.56	NIST
ΔfusH	7.60	kJ/mol	164.60	NIST
ΔfusH	7.60	kJ/mol	164.60	NIST
ΔvapH	[27.90; 31.20]	kJ/mol	[306.50; 355.50]
ΔvapH	30.40	kJ/mol	306.50	NIST
ΔvapH	30.00	kJ/mol	310.00	NIST
ΔvapH	29.90	kJ/mol	314.00	NIST
ΔvapH	30.20	kJ/mol	319.00	NIST
ΔvapH	27.90	kJ/mol	328.00	NIST
ΔvapH	27.94	kJ/mol	328.30	NIST
ΔvapH	29.60	kJ/mol	340.00	NIST
ΔvapH	31.20	kJ/mol	355.50	NIST
ν	[0.0000004; 0.0000005]	m2/s	[283.15; 313.15]
ν	0.0000005	m2/s	283.15	Kinematic Viscosities for Ether + Alkane Mixtures: Experimental Results and UNIFAC-VISCO Parameters
ν	0.0000005	m2/s	298.15	Kinematic Viscosities for Ether + Alkane Mixtures: Experimental Results and UNIFAC-VISCO Parameters
ν	0.0000004	m2/s	313.15	Kinematic Viscosities for Ether + Alkane Mixtures: Experimental Results and UNIFAC-VISCO Parameters
Pvap	[6.24; 221.79]	kPa	[263.15; 354.82]
Pvap	6.25	kPa	263.15	Thermodynamics of isomeric hexynes +MTBE binary mixtures
Pvap	6.24	kPa	263.15	Isothermal (vapor + liquid) equilibria and excess enthalpy data of {1-hexene + methyl butyl ether (MBE)} and {1-hexene + methyl tert-butyl ether (MTBE)} binary systems at several temperatures
Pvap	6.40	kPa	263.53	Isothermal (vapor + liquid) equilibria and excess enthalpy data of {1-hexene + methyl butyl ether (MBE)} and {1-hexene + methyl tert-butyl ether (MTBE)} binary systems at several temperatures
Pvap	10.64	kPa	273.15	Thermodynamics of isomeric hexynes +MTBE binary mixtures
Pvap	10.67	kPa	273.15	Isothermal (vapor + liquid) equilibria and excess enthalpy data of {1-hexene + methyl butyl ether (MBE)} and {1-hexene + methyl tert-butyl ether (MTBE)} binary systems at several temperatures
Pvap	10.80	kPa	273.34	Isothermal (vapor + liquid) equilibria and excess enthalpy data of {1-hexene + methyl butyl ether (MBE)} and {1-hexene + methyl tert-butyl ether (MTBE)} binary systems at several temperatures
Pvap	11.59	kPa	274.90	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	11.59	kPa	274.91	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	17.41	kPa	283.15	Isothermal (vapor + liquid) equilibria and excess enthalpy data of {1-hexene + methyl butyl ether (MBE)} and {1-hexene + methyl tert-butyl ether (MTBE)} binary systems at several temperatures
Pvap	17.31	kPa	283.15	Thermodynamics of isomeric hexynes +MTBE binary mixtures
Pvap	17.60	kPa	283.27	Isothermal (vapor + liquid) equilibria and excess enthalpy data of {1-hexene + methyl butyl ether (MBE)} and {1-hexene + methyl tert-butyl ether (MTBE)} binary systems at several temperatures
Pvap	17.79	kPa	283.60	A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
Pvap	18.55	kPa	284.82	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	22.07	kPa	288.60	A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
Pvap	27.25	kPa	293.15	Isothermal (vapor + liquid) equilibria and excess enthalpy data of {1-hexene + methyl butyl ether (MBE)} and {1-hexene + methyl tert-butyl ether (MTBE)} binary systems at several temperatures
Pvap	27.06	kPa	293.15	Thermodynamics of isomeric hexynes +MTBE binary mixtures
Pvap	27.40	kPa	293.25	Isothermal (vapor + liquid) equilibria and excess enthalpy data of {1-hexene + methyl butyl ether (MBE)} and {1-hexene + methyl tert-butyl ether (MTBE)} binary systems at several temperatures
Pvap	27.43	kPa	293.50	A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
Pvap	28.78	kPa	294.80	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	28.78	kPa	294.80	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	28.78	kPa	294.81	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	33.20	kPa	298.15	NCMS SOLV-DB
Pvap	33.39	kPa	298.15	Thermodynamics of isomeric hexynes +MTBE binary mixtures
Pvap	33.72	kPa	298.40	A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
Pvap	41.16	kPa	303.15	Isothermal (vapor + liquid) equilibria and excess enthalpy data of {1-hexene + methyl butyl ether (MBE)} and {1-hexene + methyl tert-butyl ether (MTBE)} binary systems at several temperatures
Pvap	40.86	kPa	303.15	Thermodynamics of isomeric hexynes +MTBE binary mixtures
Pvap	41.20	kPa	303.22	Isothermal (vapor + liquid) equilibria and excess enthalpy data of {1-hexene + methyl butyl ether (MBE)} and {1-hexene + methyl tert-butyl ether (MTBE)} binary systems at several temperatures
Pvap	41.10	kPa	303.30	A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
Pvap	43.26	kPa	304.79	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	43.24	kPa	304.79	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	49.80	kPa	308.20	A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
Pvap	59.90	kPa	313.10	A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
Pvap	59.81	kPa	313.15	Thermodynamics of isomeric hexynes +MTBE binary mixtures
Pvap	60.22	kPa	313.15	Isothermal (vapor + liquid) equilibria and excess enthalpy data of {1-hexene + methyl butyl ether (MBE)} and {1-hexene + methyl tert-butyl ether (MTBE)} binary systems at several temperatures
Pvap	62.40	kPa	313.20	Isothermal vapor-liquid equilibrium of binary and ternary systems of anisole, hexane, and toluene and ternary system of methyl tert-butyl ether, hexane, and toluene
Pvap	60.30	kPa	313.24	Isothermal (vapor + liquid) equilibria and excess enthalpy data of {1-hexene + methyl butyl ether (MBE)} and {1-hexene + methyl tert-butyl ether (MTBE)} binary systems at several temperatures
Pvap	62.95	kPa	314.75	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	62.97	kPa	314.76	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	62.97	kPa	314.76	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	71.61	kPa	318.10	A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
Pvap	85.01	kPa	323.00	A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
Pvap	85.65	kPa	323.15	Isothermal (vapor + liquid) equilibria and excess enthalpy data of {1-hexene + methyl butyl ether (MBE)} and {1-hexene + methyl tert-butyl ether (MTBE)} binary systems at several temperatures
Pvap	85.15	kPa	323.15	Thermodynamics of isomeric hexynes +MTBE binary mixtures
Pvap	85.80	kPa	323.21	Isothermal (vapor + liquid) equilibria and excess enthalpy data of {1-hexene + methyl butyl ether (MBE)} and {1-hexene + methyl tert-butyl ether (MTBE)} binary systems at several temperatures
Pvap	89.69	kPa	324.90	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	89.66	kPa	324.90	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	100.34	kPa	327.90	A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
Pvap	117.70	kPa	332.90	A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
Pvap	118.27	kPa	333.15	Thermodynamics of isomeric hexynes +MTBE binary mixtures
Pvap	120.40	kPa	333.15	Thermodynamics of binary mixtures containing N-methyl-2-pyrrolidinone VLE measurements for systems with ethers Comparison with the Mod. UNIFAC (Do) and DISQUAC models Predictions for VLE, GE m, HEm and SLE?
Pvap	118.78	kPa	333.15	Isothermal (vapor + liquid) equilibria and excess enthalpy data of {1-hexene + methyl butyl ether (MBE)} and {1-hexene + methyl tert-butyl ether (MTBE)} binary systems at several temperatures
Pvap	119.20	kPa	333.19	Isothermal (vapor + liquid) equilibria and excess enthalpy data of {1-hexene + methyl butyl ether (MBE)} and {1-hexene + methyl tert-butyl ether (MTBE)} binary systems at several temperatures
Pvap	124.02	kPa	334.85	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	137.39	kPa	337.80	A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
Pvap	160.66	kPa	343.15	Thermodynamics of isomeric hexynes +MTBE binary mixtures
Pvap	167.14	kPa	344.84	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	167.57	kPa	344.85	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	221.79	kPa	354.82	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	221.39	kPa	354.82	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
n0	[1.36594; 1.36980]		[293.15; 298.20]
n0	1.36900		293.15	(Vapor + liquid) equilibrium of the binary mixtures formed by acetonitrile with selected compounds at 95.5 kPa
n0	1.36890		293.15	A novel static analytical apparatus for phase equilibrium measurements
n0	1.36980		293.15	Vapor-Liquid Equilibrium Measurements of MTBE and TAME with Toluene
n0	1.36610		298.15	sothermal and Isobaric Vapor-Liquid Equilibrium and Excess Molar Enthalpy of the Binary Mixtures of 2-Methoxy-2-methylpropane + 2-Methyl-2-butanol or + 2-Butanol
n0	1.36648		298.15	Volumetric behaviour of binary liquid systems composed of toluene, isooctane, and methyl tert-butyl ether at temperatures from (298.15 to 328.15) K
n0	1.36648		298.15	Volumetric behavior of the ternary system (methyl tert-butyl ether + methylbenzene + butan-1-ol) and its binary sub-system (methyl tert-butyl ether + butan-1-ol) within the temperature range (298.15 to 328.15) K
n0	1.36766		298.15	Phase equilibria and interfacial tensions in the systems methyl tert-butyl ether + acetone + cyclohexane, methyl tert-butyl ether + acetone and methyl tert-butyl ether + cyclohexane
n0	1.36594		298.15	Quaternary, Ternary, and Binary LLE Measurements for 2-Methoxy-2-methylpropane + Furfural + Acetic Acid + Water at Temperatures between 298 and 307 K
n0	1.36600		298.15	Solubility of a-Carotene in Binary Solvents Formed by Some Hydrocarbons with tert-Butyl Methyl Ether and with tert-Amyl Methyl Ether
n0	1.36764		298.15	Atmospheric densities and interfacial tensions for 1- alkanol (1-butanol to 1-octanol) + water and ether (MTBE, ETBE, DIPE, TAME and THP) + water demixed mixtures.
n0	1.36640		298.15	Distribution of Butyric Acid between Water and Several Solvents
n0	1.36628		298.15	Isobaric Vapor-Liquid Equilibria at 101.32 kPa and Densities, Speeds of Sound, and Refractive Indices at 298.15 K for MTBE or DIPE or TAME + 1-Propanol Binary Systems
n0	1.36766		298.15	Vapor-Liquid Equilibria and Interfacial Tensions of the System Ethanol + 2-Methoxy-2-methylpropane
n0	1.36900		298.15	NCMS SOLV-DB
n0	1.36632		298.20	Vapor-Liquid Equilibrium Measurements of Ether Alcohol Blends for Investigation on Reformulated Gas
ρl	[713.96; 761.34]	kg/m3	[273.15; 318.15]
ρl	761.30	kg/m3	273.15	Physicochemical Properties of LiFSI Solutions II: LiFSI with Water, MTBE, and Anisole
ρl	761.34	kg/m3	273.15	Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
ρl	756.14	kg/m3	278.15	Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
ρl	751.02	kg/m3	283.15	Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
ρl	745.85	kg/m3	288.15	Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
ρl	745.90	kg/m3	288.15	Physicochemical Properties of LiFSI Solutions II: LiFSI with Water, MTBE, and Anisole
ρl	740.65	kg/m3	293.15	Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
ρl	739.80	kg/m3	293.15	Measurements of Liquid Liquid Equilibria for the Quaternary System 2-Methoxy-2-methylpropane + Phenol + Hydroquinone + Water at 313.15 K
ρl	739.45	kg/m3	293.20	Liquid-liquid equilibrium data and thermophysical properties for ternary systems composed of water, acetic acid and different solvents
ρl	735.99	kg/m3	298.15	Excess molar enthalpies of the ternary mixtures: {tetrahydrofuran or 2-methyltetrahydrofuran + methyl tert-butyl ether + n-dodecane} at the temperature 298.15 K
ρl	735.35	kg/m3	298.15	Mixing Properties for the Ternary Mixture Methyl tert-Butyl Ether + 1-Butanol + Decane at 298.15 K
ρl	735.69	kg/m3	298.15	Excess molar enthalpies of the ternary mixtures: methyl tert-butyl ether + 3-methylpentane + (n-decane or n-dodecane) at 298.15K
ρl	735.99	kg/m3	298.15	Excess molar enthalpies of the ternary mixtures (1-hexene + tetrahydrofuran or 2-methyltetrahydrofuran + methyl tert-butyl ether) at the temperature 298.15K.
ρl	735.99	kg/m3	298.15	Excess molar enthalpies of the ternary mixtures: (tetrahydrofuran or 2-methyltetrahydrofuran + methyl tert-butyl ether + n-octane) at the temperature 298.15 K
ρl	735.00	kg/m3	298.15	Physicochemical Properties of LiFSI Solutions II: LiFSI with Water, MTBE, and Anisole
ρl	735.40	kg/m3	298.15	Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
ρl	735.69	kg/m3	298.15	Excess molar enthalpies of the ternary mixtures: methyl tert-butyl ether +2-methylpentane + (n-decane or n-dodecane) at the temperature 298.15 K
ρl	735.48	kg/m3	298.15	Excess Molar Volumes and Surface Tensions of Xylene with Isopropyl Ether or Methyl tert-Butyl Ether at 298.15 K
ρl	740.60	kg/m3	298.15	Vapor-Liquid Equilibria for the Ternary Systems of Methyl tert-Butyl Ether + Methanol + Methylcyclohexane and Methyl tert-Butyl Ether + Methanol + n-Heptane and Constituent Binary Systems at 313.15 K
ρl	735.21	kg/m3	298.15	Excess Volumes of Ternary Mixtures 2,2,4-Trimethylpentane + Diisopropyl Ether or Methyl tert-Butyl Ether + Methanol, Ethanol, or 1-Propanol at 298.15 K
ρl	735.40	kg/m3	298.15	Phase equilibria for binary systems of octane boosters with 2,2,4-trimethylpentane
ρl	734.10	kg/m3	298.15	Solubility and solution thermodynamics of sorbic acid in eight pure organic solvents
ρl	735.36	kg/m3	298.15	Densities and derived thermodynamic properties of the binary systems of 1,1-dimethylethyl methyl ether with allyl methacrylate, butyl methacrylate, methacrylic acid, and vinyl acetate at T = (298.15 and 308.15) K
ρl	737.80	kg/m3	298.20	Phase equilibria of (water + propionic acid or butyric acid + 2-methoxy- 2-methylpropane) ternary systems at 298.2 K and 323.2 K
ρl	730.10	kg/m3	303.15	Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
ρl	724.85	kg/m3	308.15	Densities and derived thermodynamic properties of the binary systems of 1,1-dimethylethyl methyl ether with allyl methacrylate, butyl methacrylate, methacrylic acid, and vinyl acetate at T = (298.15 and 308.15) K
ρl	724.60	kg/m3	308.15	Physicochemical Properties of LiFSI Solutions II: LiFSI with Water, MTBE, and Anisole
ρl	724.82	kg/m3	308.15	Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
ρl	719.42	kg/m3	313.15	Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
ρl	718.08	kg/m3	313.20	Liquid-liquid equilibrium data and thermophysical properties for ternary systems composed of water, acetic acid and different solvents
ρl	713.96	kg/m3	318.15	Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
ΔfusS	[46.18; 46.18]	J/mol×K	[164.56; 164.56]
ΔfusS	46.18	J/mol×K	164.56	NIST
ΔfusS	46.18	J/mol×K	164.56	NIST
csound,fluid	[103.70; 1086.92]	m/s	[288.15; 493.06]
csound,fluid	1086.62	m/s	288.15	Mixing Properties for Binary Liquid Mixtures of Methyl tert-Butyl Ether with Propylamine and Dipropylamine at Temperatures from (288.15 to 308.15) K
csound,fluid	1082.11	m/s	288.15	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	1083.38	m/s	288.15	Influence of temperature on thermodynamics of ethers + xylenes
csound,fluid	1083.38	m/s	288.15	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	1082.40	m/s	288.15	Excess enthalpy, density, and speed of sound determination for the ternary mixture (methyl tert-butyl ether + 1-butanol + n-hexane)
csound,fluid	1086.92	m/s	288.15	Mixing Properties for Binary Liquid Mixtures of Methyl tert-Butyl Ether with Propylamine and Dipropylamine at Temperatures from (288.15 to 308.15) K
csound,fluid	1071.61	m/s	290.65	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	1070.62	m/s	290.65	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	1071.61	m/s	290.65	Influence of temperature on thermodynamics of ethers + xylenes
csound,fluid	1060.05	m/s	293.15	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	1059.40	m/s	293.15	Excess enthalpy, density, and speed of sound determination for the ternary mixture (methyl tert-butyl ether + 1-butanol + n-hexane)
csound,fluid	1063.43	m/s	293.15	Mixing Properties for Binary Liquid Mixtures of Methyl tert-Butyl Ether with Propylamine and Dipropylamine at Temperatures from (288.15 to 308.15) K
csound,fluid	1060.05	m/s	293.15	Influence of temperature on thermodynamics of ethers + xylenes
csound,fluid	1059.10	m/s	293.15	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	1048.48	m/s	295.65	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	1047.83	m/s	295.65	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	1048.48	m/s	295.65	Influence of temperature on thermodynamics of ethers + xylenes
csound,fluid	1040.35	m/s	298.15	Mixing Properties for Binary Liquid Mixtures of Methyl tert-Butyl Ether with Propylamine and Dipropylamine at Temperatures from (288.15 to 308.15) K
csound,fluid	1036.10	m/s	298.15	Excess enthalpy, density, and speed of sound determination for the ternary mixture (methyl tert-butyl ether + 1-butanol + n-hexane)
csound,fluid	1036.94	m/s	298.15	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	1036.94	m/s	298.15	Influence of temperature on thermodynamics of ethers + xylenes
csound,fluid	1036.63	m/s	298.15	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	1025.38	m/s	300.65	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	1025.42	m/s	300.65	Influence of temperature on thermodynamics of ethers + xylenes
csound,fluid	1025.42	m/s	300.65	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	1024.33	m/s	301.65	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	1012.81	m/s	303.15	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	1017.42	m/s	303.15	Mixing Properties for Binary Liquid Mixtures of Methyl tert-Butyl Ether with Propylamine and Dipropylamine at Temperatures from (288.15 to 308.15) K
csound,fluid	1013.90	m/s	303.15	Influence of temperature on thermodynamics of ethers + xylenes
csound,fluid	1014.04	m/s	303.15	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	1013.00	m/s	303.15	Excess enthalpy, density, and speed of sound determination for the ternary mixture (methyl tert-butyl ether + 1-butanol + n-hexane)
csound,fluid	1013.90	m/s	303.15	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	1024.70	m/s	303.19	Speed of Sound Measurements of 2-Methoxy-2-methylpropane in the Temperature Range of 293.15 and 673.15 K and for Pressures up to 10 MPa
csound,fluid	1002.41	m/s	305.65	Influence of temperature on thermodynamics of ethers + xylenes
csound,fluid	1001.35	m/s	305.65	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	1002.70	m/s	305.65	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	1002.41	m/s	305.65	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	990.99	m/s	308.15	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	990.10	m/s	308.15	Excess enthalpy, density, and speed of sound determination for the ternary mixture (methyl tert-butyl ether + 1-butanol + n-hexane)
csound,fluid	990.99	m/s	308.15	Influence of temperature on thermodynamics of ethers + xylenes
csound,fluid	989.90	m/s	308.15	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	991.34	m/s	308.15	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	994.68	m/s	308.15	Mixing Properties for Binary Liquid Mixtures of Methyl tert-Butyl Ether with Propylamine and Dipropylamine at Temperatures from (288.15 to 308.15) K
csound,fluid	988.60	m/s	308.16	Speed of Sound Measurements of 2-Methoxy-2-methylpropane in the Temperature Range of 293.15 and 673.15 K and for Pressures up to 10 MPa
csound,fluid	978.47	m/s	310.65	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	980.00	m/s	310.65	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	979.62	m/s	310.65	Influence of temperature on thermodynamics of ethers + xylenes
csound,fluid	979.62	m/s	310.65	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	960.40	m/s	313.08	Speed of Sound Measurements of 2-Methoxy-2-methylpropane in the Temperature Range of 293.15 and 673.15 K and for Pressures up to 10 MPa
csound,fluid	967.03	m/s	313.15	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	968.16	m/s	313.15	Influence of temperature on thermodynamics of ethers + xylenes
csound,fluid	968.16	m/s	313.15	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	968.63	m/s	313.15	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	956.80	m/s	315.65	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	956.80	m/s	315.65	Influence of temperature on thermodynamics of ethers + xylenes
csound,fluid	957.31	m/s	315.65	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	955.73	m/s	315.65	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	944.34	m/s	318.15	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	946.03	m/s	318.15	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	945.54	m/s	318.15	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	945.54	m/s	318.15	Influence of temperature on thermodynamics of ethers + xylenes
csound,fluid	942.70	m/s	318.19	Speed of Sound Measurements of 2-Methoxy-2-methylpropane in the Temperature Range of 293.15 and 673.15 K and for Pressures up to 10 MPa
csound,fluid	934.24	m/s	320.65	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	934.24	m/s	320.65	Influence of temperature on thermodynamics of ethers + xylenes
csound,fluid	934.76	m/s	320.65	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	933.01	m/s	320.65	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	912.40	m/s	323.07	Speed of Sound Measurements of 2-Methoxy-2-methylpropane in the Temperature Range of 293.15 and 673.15 K and for Pressures up to 10 MPa
csound,fluid	923.46	m/s	323.15	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	922.97	m/s	323.15	Influence of temperature on thermodynamics of ethers + xylenes
csound,fluid	921.93	m/s	323.15	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	922.97	m/s	323.15	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	904.70	m/s	328.21	Speed of Sound Measurements of 2-Methoxy-2-methylpropane in the Temperature Range of 293.15 and 673.15 K and for Pressures up to 10 MPa
csound,fluid	876.80	m/s	333.13	Speed of Sound Measurements of 2-Methoxy-2-methylpropane in the Temperature Range of 293.15 and 673.15 K and for Pressures up to 10 MPa
csound,fluid	855.10	m/s	338.07	Speed of Sound Measurements of 2-Methoxy-2-methylpropane in the Temperature Range of 293.15 and 673.15 K and for Pressures up to 10 MPa
csound,fluid	826.30	m/s	343.12	Speed of Sound Measurements of 2-Methoxy-2-methylpropane in the Temperature Range of 293.15 and 673.15 K and for Pressures up to 10 MPa
csound,fluid	797.50	m/s	348.24	Speed of Sound Measurements of 2-Methoxy-2-methylpropane in the Temperature Range of 293.15 and 673.15 K and for Pressures up to 10 MPa
csound,fluid	781.50	m/s	353.11	Speed of Sound Measurements of 2-Methoxy-2-methylpropane in the Temperature Range of 293.15 and 673.15 K and for Pressures up to 10 MPa
csound,fluid	748.60	m/s	358.22	Speed of Sound Measurements of 2-Methoxy-2-methylpropane in the Temperature Range of 293.15 and 673.15 K and for Pressures up to 10 MPa
csound,fluid	727.10	m/s	363.16	Speed of Sound Measurements of 2-Methoxy-2-methylpropane in the Temperature Range of 293.15 and 673.15 K and for Pressures up to 10 MPa
csound,fluid	707.10	m/s	368.17	Speed of Sound Measurements of 2-Methoxy-2-methylpropane in the Temperature Range of 293.15 and 673.15 K and for Pressures up to 10 MPa
csound,fluid	698.90	m/s	373.05	Speed of Sound Measurements of 2-Methoxy-2-methylpropane in the Temperature Range of 293.15 and 673.15 K and for Pressures up to 10 MPa
csound,fluid	668.30	m/s	378.05	Speed of Sound Measurements of 2-Methoxy-2-methylpropane in the Temperature Range of 293.15 and 673.15 K and for Pressures up to 10 MPa
csound,fluid	646.40	m/s	383.08	Speed of Sound Measurements of 2-Methoxy-2-methylpropane in the Temperature Range of 293.15 and 673.15 K and for Pressures up to 10 MPa
csound,fluid	627.50	m/s	388.11	Speed of Sound Measurements of 2-Methoxy-2-methylpropane in the Temperature Range of 293.15 and 673.15 K and for Pressures up to 10 MPa
csound,fluid	609.10	m/s	393.16	Speed of Sound Measurements of 2-Methoxy-2-methylpropane in the Temperature Range of 293.15 and 673.15 K and for Pressures up to 10 MPa
csound,fluid	580.10	m/s	398.11	Speed of Sound Measurements of 2-Methoxy-2-methylpropane in the Temperature Range of 293.15 and 673.15 K and for Pressures up to 10 MPa
csound,fluid	558.00	m/s	403.24	Speed of Sound Measurements of 2-Methoxy-2-methylpropane in the Temperature Range of 293.15 and 673.15 K and for Pressures up to 10 MPa
csound,fluid	537.60	m/s	408.23	Speed of Sound Measurements of 2-Methoxy-2-methylpropane in the Temperature Range of 293.15 and 673.15 K and for Pressures up to 10 MPa
csound,fluid	515.80	m/s	413.20	Speed of Sound Measurements of 2-Methoxy-2-methylpropane in the Temperature Range of 293.15 and 673.15 K and for Pressures up to 10 MPa
csound,fluid	494.40	m/s	418.24	Speed of Sound Measurements of 2-Methoxy-2-methylpropane in the Temperature Range of 293.15 and 673.15 K and for Pressures up to 10 MPa
csound,fluid	476.00	m/s	423.15	Speed of Sound Measurements of 2-Methoxy-2-methylpropane in the Temperature Range of 293.15 and 673.15 K and for Pressures up to 10 MPa
csound,fluid	453.80	m/s	428.24	Speed of Sound Measurements of 2-Methoxy-2-methylpropane in the Temperature Range of 293.15 and 673.15 K and for Pressures up to 10 MPa
csound,fluid	430.30	m/s	433.05	Speed of Sound Measurements of 2-Methoxy-2-methylpropane in the Temperature Range of 293.15 and 673.15 K and for Pressures up to 10 MPa
csound,fluid	405.80	m/s	438.19	Speed of Sound Measurements of 2-Methoxy-2-methylpropane in the Temperature Range of 293.15 and 673.15 K and for Pressures up to 10 MPa
csound,fluid	387.30	m/s	443.09	Speed of Sound Measurements of 2-Methoxy-2-methylpropane in the Temperature Range of 293.15 and 673.15 K and for Pressures up to 10 MPa
csound,fluid	360.30	m/s	448.23	Speed of Sound Measurements of 2-Methoxy-2-methylpropane in the Temperature Range of 293.15 and 673.15 K and for Pressures up to 10 MPa
csound,fluid	339.50	m/s	453.10	Speed of Sound Measurements of 2-Methoxy-2-methylpropane in the Temperature Range of 293.15 and 673.15 K and for Pressures up to 10 MPa
csound,fluid	313.60	m/s	458.19	Speed of Sound Measurements of 2-Methoxy-2-methylpropane in the Temperature Range of 293.15 and 673.15 K and for Pressures up to 10 MPa
csound,fluid	287.10	m/s	463.23	Speed of Sound Measurements of 2-Methoxy-2-methylpropane in the Temperature Range of 293.15 and 673.15 K and for Pressures up to 10 MPa
csound,fluid	265.00	m/s	468.18	Speed of Sound Measurements of 2-Methoxy-2-methylpropane in the Temperature Range of 293.15 and 673.15 K and for Pressures up to 10 MPa
csound,fluid	236.50	m/s	473.17	Speed of Sound Measurements of 2-Methoxy-2-methylpropane in the Temperature Range of 293.15 and 673.15 K and for Pressures up to 10 MPa
csound,fluid	206.10	m/s	478.08	Speed of Sound Measurements of 2-Methoxy-2-methylpropane in the Temperature Range of 293.15 and 673.15 K and for Pressures up to 10 MPa
csound,fluid	177.70	m/s	483.20	Speed of Sound Measurements of 2-Methoxy-2-methylpropane in the Temperature Range of 293.15 and 673.15 K and for Pressures up to 10 MPa
csound,fluid	142.80	m/s	488.11	Speed of Sound Measurements of 2-Methoxy-2-methylpropane in the Temperature Range of 293.15 and 673.15 K and for Pressures up to 10 MPa
csound,fluid	103.70	m/s	493.06	Speed of Sound Measurements of 2-Methoxy-2-methylpropane in the Temperature Range of 293.15 and 673.15 K and for Pressures up to 10 MPa
γ	[0.01; 0.02]	N/m	[243.08; 393.13]
γ	0.02	N/m	243.08	Surface Tension of Dimethoxymethane and Methyl tert-Butyl Ether
γ	0.02	N/m	248.01	Surface Tension of Dimethoxymethane and Methyl tert-Butyl Ether
γ	0.02	N/m	253.11	Surface Tension of Dimethoxymethane and Methyl tert-Butyl Ether
γ	0.02	N/m	258.13	Surface Tension of Dimethoxymethane and Methyl tert-Butyl Ether
γ	0.02	N/m	263.10	Surface Tension of Dimethoxymethane and Methyl tert-Butyl Ether
γ	0.02	N/m	268.13	Surface Tension of Dimethoxymethane and Methyl tert-Butyl Ether
γ	0.02	N/m	273.16	Surface Tension of Dimethoxymethane and Methyl tert-Butyl Ether
γ	0.02	N/m	278.11	Surface Tension of Dimethoxymethane and Methyl tert-Butyl Ether
γ	0.02	N/m	283.12	Surface Tension of Dimethoxymethane and Methyl tert-Butyl Ether
γ	0.02	N/m	288.13	Surface Tension of Dimethoxymethane and Methyl tert-Butyl Ether
γ	0.02	N/m	293.07	Surface Tension of Dimethoxymethane and Methyl tert-Butyl Ether
γ	0.02	N/m	298.08	Surface Tension of Dimethoxymethane and Methyl tert-Butyl Ether
γ	0.02	N/m	298.15	NCMS SOLV-DB
γ	0.02	N/m	303.11	Surface Tension of Dimethoxymethane and Methyl tert-Butyl Ether
γ	0.02	N/m	308.15	Surface Tension of Dimethoxymethane and Methyl tert-Butyl Ether
γ	0.02	N/m	313.16	Surface Tension of Dimethoxymethane and Methyl tert-Butyl Ether
γ	0.02	N/m	318.11	Surface Tension of Dimethoxymethane and Methyl tert-Butyl Ether
γ	0.02	N/m	323.16	Surface Tension of Dimethoxymethane and Methyl tert-Butyl Ether
γ	0.01	N/m	328.14	Surface Tension of Dimethoxymethane and Methyl tert-Butyl Ether
γ	0.01	N/m	333.15	Surface Tension of Dimethoxymethane and Methyl tert-Butyl Ether
γ	0.01	N/m	338.16	Surface Tension of Dimethoxymethane and Methyl tert-Butyl Ether
γ	0.01	N/m	343.13	Surface Tension of Dimethoxymethane and Methyl tert-Butyl Ether
γ	0.01	N/m	348.13	Surface Tension of Dimethoxymethane and Methyl tert-Butyl Ether
γ	0.01	N/m	353.13	Surface Tension of Dimethoxymethane and Methyl tert-Butyl Ether
γ	0.01	N/m	358.15	Surface Tension of Dimethoxymethane and Methyl tert-Butyl Ether
γ	0.01	N/m	363.13	Surface Tension of Dimethoxymethane and Methyl tert-Butyl Ether
γ	0.01	N/m	368.13	Surface Tension of Dimethoxymethane and Methyl tert-Butyl Ether
γ	0.01	N/m	373.12	Surface Tension of Dimethoxymethane and Methyl tert-Butyl Ether
γ	0.01	N/m	378.12	Surface Tension of Dimethoxymethane and Methyl tert-Butyl Ether
γ	0.01	N/m	383.12	Surface Tension of Dimethoxymethane and Methyl tert-Butyl Ether
γ	0.01	N/m	388.14	Surface Tension of Dimethoxymethane and Methyl tert-Butyl Ether
γ	0.01	N/m	393.13	Surface Tension of Dimethoxymethane and Methyl tert-Butyl Ether
αdiff	[2.73e-08; 6.40e-08]	m2/s	[303.15; 493.15]
αdiff	6.40e-08	m2/s	303.15	Thermal Diffusivity of 2-Methoxy-2-methylpropane at Temperatures from (303.15 to 493.15) K and Pressures from (1.5 to 10) MPa
αdiff	6.17e-08	m2/s	313.15	Thermal Diffusivity of 2-Methoxy-2-methylpropane at Temperatures from (303.15 to 493.15) K and Pressures from (1.5 to 10) MPa
αdiff	5.87e-08	m2/s	323.15	Thermal Diffusivity of 2-Methoxy-2-methylpropane at Temperatures from (303.15 to 493.15) K and Pressures from (1.5 to 10) MPa
αdiff	5.70e-08	m2/s	333.15	Thermal Diffusivity of 2-Methoxy-2-methylpropane at Temperatures from (303.15 to 493.15) K and Pressures from (1.5 to 10) MPa
αdiff	5.42e-08	m2/s	343.15	Thermal Diffusivity of 2-Methoxy-2-methylpropane at Temperatures from (303.15 to 493.15) K and Pressures from (1.5 to 10) MPa
αdiff	5.26e-08	m2/s	353.15	Thermal Diffusivity of 2-Methoxy-2-methylpropane at Temperatures from (303.15 to 493.15) K and Pressures from (1.5 to 10) MPa
αdiff	5.05e-08	m2/s	363.15	Thermal Diffusivity of 2-Methoxy-2-methylpropane at Temperatures from (303.15 to 493.15) K and Pressures from (1.5 to 10) MPa
αdiff	4.83e-08	m2/s	373.15	Thermal Diffusivity of 2-Methoxy-2-methylpropane at Temperatures from (303.15 to 493.15) K and Pressures from (1.5 to 10) MPa
αdiff	4.72e-08	m2/s	383.15	Thermal Diffusivity of 2-Methoxy-2-methylpropane at Temperatures from (303.15 to 493.15) K and Pressures from (1.5 to 10) MPa
αdiff	4.64e-08	m2/s	393.15	Thermal Diffusivity of 2-Methoxy-2-methylpropane at Temperatures from (303.15 to 493.15) K and Pressures from (1.5 to 10) MPa
αdiff	4.55e-08	m2/s	403.15	Thermal Diffusivity of 2-Methoxy-2-methylpropane at Temperatures from (303.15 to 493.15) K and Pressures from (1.5 to 10) MPa
αdiff	4.48e-08	m2/s	413.15	Thermal Diffusivity of 2-Methoxy-2-methylpropane at Temperatures from (303.15 to 493.15) K and Pressures from (1.5 to 10) MPa
αdiff	4.38e-08	m2/s	423.15	Thermal Diffusivity of 2-Methoxy-2-methylpropane at Temperatures from (303.15 to 493.15) K and Pressures from (1.5 to 10) MPa
αdiff	4.31e-08	m2/s	433.15	Thermal Diffusivity of 2-Methoxy-2-methylpropane at Temperatures from (303.15 to 493.15) K and Pressures from (1.5 to 10) MPa
αdiff	4.18e-08	m2/s	443.15	Thermal Diffusivity of 2-Methoxy-2-methylpropane at Temperatures from (303.15 to 493.15) K and Pressures from (1.5 to 10) MPa
αdiff	4.05e-08	m2/s	453.15	Thermal Diffusivity of 2-Methoxy-2-methylpropane at Temperatures from (303.15 to 493.15) K and Pressures from (1.5 to 10) MPa
αdiff	3.91e-08	m2/s	458.15	Thermal Diffusivity of 2-Methoxy-2-methylpropane at Temperatures from (303.15 to 493.15) K and Pressures from (1.5 to 10) MPa
αdiff	3.86e-08	m2/s	463.15	Thermal Diffusivity of 2-Methoxy-2-methylpropane at Temperatures from (303.15 to 493.15) K and Pressures from (1.5 to 10) MPa
αdiff	3.66e-08	m2/s	468.15	Thermal Diffusivity of 2-Methoxy-2-methylpropane at Temperatures from (303.15 to 493.15) K and Pressures from (1.5 to 10) MPa
αdiff	3.55e-08	m2/s	473.15	Thermal Diffusivity of 2-Methoxy-2-methylpropane at Temperatures from (303.15 to 493.15) K and Pressures from (1.5 to 10) MPa
αdiff	3.47e-08	m2/s	475.15	Thermal Diffusivity of 2-Methoxy-2-methylpropane at Temperatures from (303.15 to 493.15) K and Pressures from (1.5 to 10) MPa
αdiff	3.36e-08	m2/s	477.15	Thermal Diffusivity of 2-Methoxy-2-methylpropane at Temperatures from (303.15 to 493.15) K and Pressures from (1.5 to 10) MPa
αdiff	3.36e-08	m2/s	479.15	Thermal Diffusivity of 2-Methoxy-2-methylpropane at Temperatures from (303.15 to 493.15) K and Pressures from (1.5 to 10) MPa
αdiff	3.30e-08	m2/s	481.15	Thermal Diffusivity of 2-Methoxy-2-methylpropane at Temperatures from (303.15 to 493.15) K and Pressures from (1.5 to 10) MPa
αdiff	3.22e-08	m2/s	483.15	Thermal Diffusivity of 2-Methoxy-2-methylpropane at Temperatures from (303.15 to 493.15) K and Pressures from (1.5 to 10) MPa
αdiff	3.07e-08	m2/s	485.15	Thermal Diffusivity of 2-Methoxy-2-methylpropane at Temperatures from (303.15 to 493.15) K and Pressures from (1.5 to 10) MPa
αdiff	3.02e-08	m2/s	487.15	Thermal Diffusivity of 2-Methoxy-2-methylpropane at Temperatures from (303.15 to 493.15) K and Pressures from (1.5 to 10) MPa
αdiff	2.95e-08	m2/s	489.15	Thermal Diffusivity of 2-Methoxy-2-methylpropane at Temperatures from (303.15 to 493.15) K and Pressures from (1.5 to 10) MPa
αdiff	2.81e-08	m2/s	491.15	Thermal Diffusivity of 2-Methoxy-2-methylpropane at Temperatures from (303.15 to 493.15) K and Pressures from (1.5 to 10) MPa
αdiff	2.73e-08	m2/s	493.15	Thermal Diffusivity of 2-Methoxy-2-methylpropane at Temperatures from (303.15 to 493.15) K and Pressures from (1.5 to 10) MPa

Datasets

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.15	100.00	750.94
288.15	100.00	745.79
293.15	100.00	740.59
298.15	100.00	735.34
303.15	100.00	730.04
308.15	100.00	724.69
313.15	100.00	719.29
318.15	100.00	713.84
323.15	100.00	708.45
283.15	5000.00	756.29
288.15	5000.00	751.33
293.15	5000.00	746.34
298.15	5000.00	741.32
303.15	5000.00	736.27
308.15	5000.00	731.19
313.15	5000.00	726.07
318.15	5000.00	720.92
323.15	5000.00	715.73
283.15	10000.00	761.29
288.15	10000.00	756.52
293.15	10000.00	751.7
298.15	10000.00	746.89
303.15	10000.00	742.05
308.15	10000.00	737.18
313.15	10000.00	732.27
318.15	10000.00	727.36
323.15	10000.00	722.39
283.15	15000.00	765.93
288.15	15000.00	761.32
293.15	15000.00	756.68
298.15	15000.00	752.04
303.15	15000.00	747.37
308.15	15000.00	742.69
313.15	15000.00	737.97
318.15	15000.00	733.26
323.15	15000.00	728.51
283.15	20000.00	770.32
288.15	20000.00	765.86
293.15	20000.00	761.35
298.15	20000.00	756.85
303.15	20000.00	752.37
308.15	20000.00	747.84
313.15	20000.00	743.29
318.15	20000.00	738.74
323.15	20000.00	734.2
283.15	25000.00	774.48
288.15	25000.00	770.15
293.15	25000.00	765.77
298.15	25000.00	761.42
303.15	25000.00	757.05
308.15	25000.00	752.67
313.15	25000.00	748.27
318.15	25000.00	743.91
323.15	25000.00	739.51
283.15	30000.00	778.47
288.15	30000.00	774.24
293.15	30000.00	770.01
298.15	30000.00	765.75
303.15	30000.00	761.51
308.15	30000.00	757.26
313.15	30000.00	752.99
318.15	30000.00	748.75
323.15	30000.00	744.49
283.15	35000.00	782.29
288.15	35000.00	778.15
293.15	35000.00	774.0
298.15	35000.00	769.88
303.15	35000.00	765.74
308.15	35000.00	761.6
313.15	35000.00	757.46
318.15	35000.00	753.35
323.15	35000.00	749.2
283.15	40000.00	785.94
288.15	40000.00	781.89
293.15	40000.00	777.85
298.15	40000.00	773.81
303.15	40000.00	769.79
308.15	40000.00	765.75
313.15	40000.00	761.71
318.15	40000.00	757.7
323.15	40000.00	753.67
283.15	45000.00	789.45
288.15	45000.00	785.49
293.15	45000.00	781.54
298.15	45000.00	777.6
303.15	45000.00	773.65
308.15	45000.00	769.71
313.15	45000.00	765.77
318.15	45000.00	761.86
323.15	45000.00	757.92
283.15	50000.00	792.86
288.15	50000.00	788.97
293.15	50000.00	785.09
298.15	50000.00	781.23
303.15	50000.00	777.36
308.15	50000.00	773.49
313.15	50000.00	769.65
318.15	50000.00	765.83
323.15	50000.00	761.98
283.15	55000.00	796.13
288.15	55000.00	792.3
293.15	55000.00	788.51
298.15	55000.00	784.71
303.15	55000.00	780.95
308.15	55000.00	777.14
313.15	55000.00	773.39
318.15	55000.00	769.63
323.15	55000.00	765.85
283.15	60000.00	799.29
288.15	60000.00	795.55
293.15	60000.00	791.81
298.15	60000.00	788.1
303.15	60000.00	784.37
308.15	60000.00	780.65
313.15	60000.00	776.97
318.15	60000.00	773.29
323.15	60000.00	769.61
283.15	65000.00	802.37
288.15	65000.00	798.67
293.15	65000.00	795.0
298.15	65000.00	791.36
303.15	65000.00	787.7
308.15	65000.00	784.04
313.15	65000.00	780.41
318.15	65000.00	776.82
323.15	65000.00	773.22
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[103.15; 343.44]	J/mol×K	[200.00; 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			8.97290e+01
Coefficient B			-6.82140e+02
Coefficient C			6.00424e+00
Coefficient D			2.14410e-05
Coefficient E			-2.01920e-08
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	103.15	J/mol×K	200.00	Calculated Property
Cp,gas	145.92	J/mol×K	344.44	Calculated Property
Cp,gas	190.68	J/mol×K	488.89	Calculated Property
Cp,gas	228.48	J/mol×K	633.33	Calculated Property
Cp,gas	259.03	J/mol×K	777.78	Calculated Property
Cp,gas	283.60	J/mol×K	922.22	Calculated Property
Cp,gas	303.44	J/mol×K	1066.67	Calculated Property
Cp,gas	319.56	J/mol×K	1211.11	Calculated Property
Cp,gas	332.71	J/mol×K	1355.56	Calculated Property
Cp,gas	343.44	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[153.84; 197.81]	J/mol×K	[164.55; 328.35]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K
Coefficient A			1.35550e+02
Coefficient B			-5.42290e+01
Coefficient C			1.74804e+00
Coefficient D			1.03290e-02
Coefficient E			-7.82060e-06
Temperature range, min.			164.55
Temperature range, max.			328.35
Cp,liquid	153.84	J/mol×K	164.55	Calculated Property
Cp,liquid	157.26	J/mol×K	182.75	Calculated Property
Cp,liquid	161.03	J/mol×K	200.95	Calculated Property
Cp,liquid	165.17	J/mol×K	219.15	Calculated Property
Cp,liquid	169.69	J/mol×K	237.35	Calculated Property
Cp,liquid	174.59	J/mol×K	255.55	Calculated Property
Cp,liquid	179.87	J/mol×K	273.75	Calculated Property
Cp,liquid	185.51	J/mol×K	291.95	Calculated Property
Cp,liquid	191.50	J/mol×K	310.15	Calculated Property
Cp,liquid	197.81	J/mol×K	328.35	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0027361; 0.0001065]	Pa×s	[180.00; 449.93]	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			-7.13600e+00
Coefficient B			8.21590e+02
Coefficient C			-6.44190e-01
Coefficient D			4.83220e-07
Coefficient E			2.00000e+00
Temperature range, min.			180.00
Temperature range, max.			449.93
η	0.0027361	Pa×s	180.00	Calculated Property
η	0.0012982	Pa×s	209.99	Calculated Property
η	0.0007353	Pa×s	239.98	Calculated Property
η	0.0004694	Pa×s	269.98	Calculated Property
η	0.0003262	Pa×s	299.97	Calculated Property
η	0.0002414	Pa×s	329.96	Calculated Property
η	0.0001873	Pa×s	359.95	Calculated Property
η	0.0001509	Pa×s	389.95	Calculated Property
η	0.0001252	Pa×s	419.94	Calculated Property
η	0.0001065	Pa×s	449.93	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[36.44; 0.00]	kJ/mol	[164.55; 497.10]	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			7.68522e+01
Coefficient B			4.56183e+00
Coefficient C			-1.20688e+01
Coefficient D			1.36123e+01
Coefficient E			-5.56912e+00
Critical temperature, Tc (K)			4.97100e+02
Temperature range, min.			164.55
Temperature range, max.			497.10
ΔvapH	36.44	kJ/mol	164.55	Calculated Property
ΔvapH	34.60	kJ/mol	201.50	Calculated Property
ΔvapH	33.08	kJ/mol	238.45	Calculated Property
ΔvapH	31.45	kJ/mol	275.40	Calculated Property
ΔvapH	29.39	kJ/mol	312.35	Calculated Property
ΔvapH	26.74	kJ/mol	349.30	Calculated Property
ΔvapH	23.48	kJ/mol	386.25	Calculated Property
ΔvapH	19.60	kJ/mol	423.20	Calculated Property
ΔvapH	14.68	kJ/mol	460.15	Calculated Property
ΔvapH	0.00	kJ/mol	497.10	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.64]	kPa	[243.08; 348.65]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.53357e+01
Coefficient B			-3.16987e+03
Coefficient C			-3.24310e+01
Temperature range, min.			243.08
Temperature range, max.			348.65
Pvap	1.33	kPa	243.08	Calculated Property
Pvap	2.95	kPa	254.81	Calculated Property
Pvap	6.02	kPa	266.54	Calculated Property
Pvap	11.49	kPa	278.27	Calculated Property
Pvap	20.67	kPa	290.00	Calculated Property
Pvap	35.34	kPa	301.73	Calculated Property
Pvap	57.76	kPa	313.46	Calculated Property
Pvap	90.75	kPa	325.19	Calculated Property
Pvap	137.73	kPa	336.92	Calculated Property
Pvap	202.64	kPa	348.65	Calculated Property
Pvap	[5.30e-04; 3287.63]	kPa	[164.55; 497.10]	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			5.64027e+01
Coefficient B			-5.32268e+03
Coefficient C			-6.21274e+00
Coefficient D			3.95114e-06
Coefficient E			2.00000e+00
Temperature range, min.			164.55
Temperature range, max.			497.10
Pvap	5.30e-04	kPa	164.55	Calculated Property
Pvap	0.06	kPa	201.50	Calculated Property
Pvap	1.34	kPa	238.45	Calculated Property
Pvap	11.83	kPa	275.40	Calculated Property
Pvap	58.01	kPa	312.35	Calculated Property
Pvap	193.49	kPa	349.30	Calculated Property
Pvap	495.52	kPa	386.25	Calculated Property
Pvap	1052.97	kPa	423.20	Calculated Property
Pvap	1955.16	kPa	460.15	Calculated Property
Pvap	3287.63	kPa	497.10	Calculated Property
Pvap	[5.51e-04; 3384.37]	kPa	[164.55; 497.10]	KDB Vapor Pressure Data
Equation			ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K
Coefficient A			6.49173e+01
Coefficient B			-5.55710e+03
Coefficient C			-7.60854e+00
Coefficient D			6.59025e-06
Coefficient E			0.00000e+00
Temperature range, min.			164.55
Temperature range, max.			497.10
Pvap	5.51e-04	kPa	164.55	Calculated Property
Pvap	0.06	kPa	201.50	Calculated Property
Pvap	1.40	kPa	238.45	Calculated Property
Pvap	12.09	kPa	275.40	Calculated Property
Pvap	58.24	kPa	312.35	Calculated Property
Pvap	191.91	kPa	349.30	Calculated Property
Pvap	489.32	kPa	386.25	Calculated Property
Pvap	1044.38	kPa	423.20	Calculated Property
Pvap	1966.13	kPa	460.15	Calculated Property
Pvap	3384.37	kPa	497.10	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[882.98; 420.27]	kg/m3	[164.55; 497.10]	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			8.92941e+01
Coefficient B			2.91190e-01
Coefficient C			5.13950e+02
Coefficient D			3.99290e-01
Comment			Range stopped at Tc; ChemSep gives it to 513.94 K.
Temperature range, min.			164.55
Temperature range, max.			497.10
ρl	882.98	kg/m3	164.55	Calculated Property
ρl	843.15	kg/m3	201.50	Calculated Property
ρl	802.37	kg/m3	238.45	Calculated Property
ρl	760.38	kg/m3	275.40	Calculated Property
ρl	716.81	kg/m3	312.35	Calculated Property
ρl	671.06	kg/m3	349.30	Calculated Property
ρl	622.22	kg/m3	386.25	Calculated Property
ρl	568.54	kg/m3	423.20	Calculated Property
ρl	506.11	kg/m3	460.15	Calculated Property
ρl	420.27	kg/m3	497.10	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 2.29e-05]	N/m	[164.55; 495.44]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K
Coefficient A			-3.28210e-02
Coefficient B			-2.93270e+01
Coefficient C			-1.98130e+00
Coefficient D			-3.27890e-03
Coefficient E			1.01440e-06
Comment			Range stopped where the equation turns negative; ChemSep gives it to 497.1 K.
Temperature range, min.			164.55
Temperature range, max.			495.44
γ	0.04	N/m	164.55	Calculated Property
γ	0.03	N/m	201.32	Calculated Property
γ	0.03	N/m	238.08	Calculated Property
γ	0.02	N/m	274.85	Calculated Property
γ	0.02	N/m	311.61	Calculated Property
γ	0.01	N/m	348.38	Calculated Property
γ	0.01	N/m	385.14	Calculated Property
γ	0.01	N/m	421.91	Calculated Property
γ	0.00	N/m	458.67	Calculated Property
γ	2.29e-05	N/m	495.44	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.00; 0.09]	W/m×K	[164.55; 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			2.30340e-04
Coefficient B			9.21280e-01
Coefficient C			3.91600e+02
Coefficient D			8.02740e+04
Temperature range, min.			164.55
Temperature range, max.			1000.00
λgas	0.00	W/m×K	164.55	Calculated Property
λgas	0.01	W/m×K	257.38	Calculated Property
λgas	0.02	W/m×K	350.21	Calculated Property
λgas	0.03	W/m×K	443.03	Calculated Property
λgas	0.04	W/m×K	535.86	Calculated Property
λgas	0.05	W/m×K	628.69	Calculated Property
λgas	0.06	W/m×K	721.52	Calculated Property
λgas	0.07	W/m×K	814.34	Calculated Property
λgas	0.08	W/m×K	907.17	Calculated Property
λgas	0.09	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.17; 0.08]	W/m×K	[164.55; 460.87]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is λliquid in W/m×K, T in K
Coefficient A			7.30080e-02
Coefficient B			3.06730e+02
Coefficient C			-6.31110e+00
Coefficient D			1.92350e-02
Coefficient E			-3.79330e-05
Temperature range, min.			164.55
Temperature range, max.			460.87
λliquid	0.17	W/m×K	164.55	Calculated Property
λliquid	0.16	W/m×K	197.47	Calculated Property
λliquid	0.15	W/m×K	230.40	Calculated Property
λliquid	0.14	W/m×K	263.32	Calculated Property
λliquid	0.13	W/m×K	296.25	Calculated Property
λliquid	0.12	W/m×K	329.17	Calculated Property
λliquid	0.10	W/m×K	362.10	Calculated Property
λliquid	0.09	W/m×K	395.02	Calculated Property
λliquid	0.09	W/m×K	427.95	Calculated Property
λliquid	0.08	W/m×K	460.87	Calculated Property

Similar Compounds

Find more compounds similar to Propane, 2-methoxy-2-methyl-.

Mixtures

• Propane, 2-methoxy-2-methyl- + Water
• 2-Propanol + Propane, 2-methoxy-2-methyl- + Water
• Propane, 2-methoxy-2-methyl- + Pentane, 3-methyl-
• Dodecane + Propane, 2-methoxy-2-methyl- + Pentane, 3-methyl-
• Decane + Propane, 2-methoxy-2-methyl- + Pentane, 3-methyl-
• Propane, 2-methoxy-2-methyl- + Pentane, 2,2,4-trimethyl-
• Toluene + Propane, 2-methoxy-2-methyl-
• Ethanol + Propane, 2-methoxy-2-methyl- + Water
• Propane, 2-methoxy-2-methyl- + Acetic acid, mercapto- + Water
• 2-Propyn-1-ol + Propane, 2-methoxy-2-methyl- + Water
• Caprolactam + Propane, 2-methoxy-2-methyl- + Cyclohexanone, oxime
• n-Butyl methacrylate + Propane, 2-methoxy-2-methyl-
• Propane, 2-methoxy-2-methyl- + 2-Propenoic acid, 2-methyl-
• Acetic acid ethenyl ester + Propane, 2-methoxy-2-methyl-
• 2-Propenoic acid, 2-methyl-, 2-propenyl ester + Propane, 2-methoxy-2-methyl-
• Caprolactam + Propane, 2-methoxy-2-methyl-
• Propane, 2-methoxy-2-methyl- + Cyclohexane
• Propane, 2-methoxy-2-methyl- + Acetone
• Propane, 2-methoxy-2-methyl- + Acetone + Cyclohexane
• n-Hexane + Propane, 2-methoxy-2-methyl- + 1-Pentanol

Find more mixtures with Propane, 2-methoxy-2-methyl-.

Sources

• KDB Vapor Pressure Data
• 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.
• PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
• 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.
• Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
• Kinematic Viscosities for Ether + Alkane Mixtures: Experimental Results and UNIFAC-VISCO Parameters
• Experimental and Predicted Viscosities of Binary Mixtures Containing Chlorinated and Oxygenated Compounds
• (Solid + liquid) phase equilibria of binary mixtures containing N-methyl-2-pyrrolidinone and ethers at atmospheric pressure
• Phase equilibria for binary systems of octane boosters with 2,2,4-trimethylpentane
• Determination of excess molar enthalpies of the ternary system methyl tert-butyl ether + 1-pentanol + nonane at 298.15K Analysis and comparison with predicted values of the UNIFAC model and some empirical methods
• Liquid-liquid equilibrium data of water with neohexane, methylcyclohexane, tert-butyl methyl ether, n-heptane and vapor -liquid-liquid equilibrium with methane
• Thermodynamics of binary mixtures containing N-methyl-2-pyrrolidinone VLE measurements for systems with ethers Comparison with the Mod. UNIFAC (Do) and DISQUAC models Predictions for VLE, GE m, HEm and SLE?
• Infinite dilution activity coefficient measurements by inert gas stripping method
• Thermodynamics of isomeric hexynes +MTBE binary mixtures
• (Liquid + liquid) equilibria for the quaternary system water + methyl tert-butyl ether + ethanol + benzene at 303.15K
• Liquid liquid equilibria for the MTBE+water + salts systems at 298.15K
• Influence of temperature on thermodynamics of ethers + xylenes
• Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
• Study of the effect of increasing the chain length of the alkane in excess molar enthalpies of mixtures containing methyl tert-butyl ether, 1-propanol, alkane
• Phase equilibria and interfacial tensions in the systems methyl tert-butyl ether + acetone + cyclohexane, methyl tert-butyl ether + acetone and methyl tert-butyl ether + cyclohexane
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium trifluoromethanesulfonate using GLC
• Isothermal vapour liquid equilibria in the binary and ternary systems composed of tert-butyl methyl ether, 3,3-dimethyl-2-butanone and 2,2-dimethyl-1-propanol
• Activity coefficients at infinite dilution measurements for organic solutes and water in the 1-hexyloxymethyl-3-methyl-imidazolium and 1,3-dihexyloxymethyl-imidazolium bis(trifluoromethylsulfonyl)-imide ionic liquids The cation influence
• Study on the effect of increasing the chain length of the alkanol in excess molar enthalpies of mixtures containing 2-methoxy-2-methylpropane, 1-alkanol, decane
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
• Solubility of caprolactam in different organic solvents
• A novel static analytical apparatus for phase equilibrium measurements
• Liquid liquid equilibria at 298.15 K for ternary mixtures of methyl tert-butyl ether + methanol (or ethanol) + imidazolium-based ionic liquids at atmospheric pressure
• Atmospheric densities and interfacial tensions for 1- alkanol (1-butanol to 1-octanol) + water and ether (MTBE, ETBE, DIPE, TAME and THP) + water demixed mixtures.
• Phase equilibria of (water + propionic acid or butyric acid + 2-methoxy- 2-methylpropane) ternary systems at 298.2 K and 323.2 K
• Determination and correlation of heat of mixing of the carbon dioxide + tert-butyl methyl ether system at 298.15 and 303.15 K and 5.0 - 7.0 MPa
• Activity coefficients at infinite dilution of organic solvents and water in 1-butyl-3-methylimidazolium dicyanamide. A literature review of hexane/hex-1-ene separation
• Experimental and modeled volumetric behavior of linear and branched ethers
• Determination and modeling for solid-liquid phase equilibrium of ternary caprolactam + cyclohexanone oxime + methyl tert-butyl ether system
• A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
• High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
• Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
• Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-butyl-1-methylpyrrolidinium dicyanamide
• New ionic liquid [P4,4,4,4][NTf2] in bio-butanol extraction on investigation of limiting activity coefficients
• Liquid-liquid equilibrium measurement and thermodynamics modeling for the systems water + thioglycolic acid + isopropyl ether/methyl tert-butyl ether at 298.15 and 308.15 K
• Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
• Liquid-liquid equilibrium data and thermophysical properties for ternary systems composed of water, acetic acid and different solvents
• Excess molar enthalpies of the ternary mixtures: methyl tert-butyl ether +2-methylpentane + (n-decane or n-dodecane) at the temperature 298.15 K
• Excess molar enthalpies of the ternary mixtures: (methyl tert-butyl ether or 2-methyltetrahydrofuran + cyclohexane + 2,2,4- trimethylpentane} at the temperature 298.15 K
• Densities and derived thermodynamic properties of the binary systems of 1,1-dimethylethyl methyl ether with allyl methacrylate, butyl methacrylate, methacrylic acid, and vinyl acetate at T = (298.15 and 308.15) K
• Excess molar enthalpies of the ternary mixtures: {tetrahydrofuran or 2-methyltetrahydrofuran + methyl tert-butyl ether + n-dodecane} at the temperature 298.15 K
• Quaternary (liquid + liquid) equilibria for (water + 1,1-dimethylethyl methyl ether + diisopropyl ether + toluene) at the temperature 298.15 K
• Quaternary (liquid + liquid) equilibria for (water + 2-propanol + 1,1-dimethylethyl methyl ether + diisopropyl ether) at the temperature 298.15 K
• Excess molar enthalpies of the ternary mixtures: (tetrahydrofuran or 2-methyltetrahydrofuran + methyl tert-butyl ether + n-octane) at the temperature 298.15 K
• (Liquid + liquid) phase equilibria of 1-alkyl-3-methylimidazolium methylsulfate with alcohols, or ethers, or ketones
• Excess molar enthalpies of the ternary mixtures (1-hexene + tetrahydrofuran or 2-methyltetrahydrofuran + methyl tert-butyl ether) at the temperature 298.15K.
• Excess enthalpy, density, and speed of sound determination for the ternary mixture (methyl tert-butyl ether + 1-butanol + n-hexane)
• (Vapor + liquid) equilibrium of the binary mixtures formed by acetonitrile with selected compounds at 95.5 kPa
• Thermodynamics of biofuels: Excess enthalpies for binary mixtures involving ethyl 1,1-dimethylethyl ether and hydrocarbons at different temperatures using a new flow calorimeter
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid triethylsulphonium bis(trifluoromethylsulfonyl)imide
• Measurements of activity coefficients at infinite dilution of aliphatic and aromatic hydrocarbons, alcohols, thiophene, tetrahydrofuran, MTBE, and water in ionic liquid [BMIM][SCN] using GLC
• Volumetric behaviour of binary liquid systems composed of toluene, isooctane, and methyl tert-butyl ether at temperatures from (298.15 to 328.15) K
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 4-methyl-N-butyl-pyridinium bis(trifluoromethylsulfonyl)-imide
• Gas liquid chromatography measurements of activity coefficients at infinite dilution of various organic solutes and water in tri-iso-butylmethylphosphonium tosylate ionic liquid
• Volumetric behaviour of the ternary liquid system composed of methyl tert-butyl ether, toluene, and isooctane at temperatures from (298.15 to 328.15) K: Experimental data and correlation
• Measurements of activity coefficients at infinite dilution of organic solutes and water in 1-propyl-1-methylpiperidinium bis{(trifluoromethyl)sulfonyl}imide ionic liquid using g.l.c.
• Measurements of activity coefficients at infinite dilution of organic compounds and water in isoquinolinium-based ionic liquid [C8iQuin][NTf2] using GLC
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
• Volumetric and viscometric properties of binary mixtures of {methyl tert-butyl ether (MTBE) + alcohol} at several temperatures and p = 0.1 MPa: Experimental results and application of the ERAS model
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(3-hydroxypropyl)pyridinium bis(trifluoromethylsulfonyl)-amide
• Thermodynamics and activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tetracyanoborate
• Interactions of volatile organic compounds with the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-hexyl-3-methylimidazolium tetracyanoborate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpiperidinium bis(trifluoromethylsulfonyl)-amide
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpyrrolidinium bis(trifluoromethylsulfonyl)-amide
• Isothermal (vapor + liquid) equilibria and excess enthalpy data of {1-hexene + methyl butyl ether (MBE)} and {1-hexene + methyl tert-butyl ether (MTBE)} binary systems at several temperatures
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium trifluorotris(perfluoroethyl)phosphate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpiperidinium trifluorotris(perfluoroethyl)phosphate
• Interactions of volatile organic compounds with the ionic liquids 1-butyl-1-methylpyrrolidinium tetracyanoborate and 1-butyl-1-methylpyrrolidinium bis(oxalato)borate
• Physicochemical properties and activity coefficients at infinite dilution for organic solutes and water in a novel bicyclic guanidinium superbase-derived protic ionic liquid
• Experimental and theoretical study on infinite dilution activity coefficients of various solutes in piperidinium ionic liquids
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpyrrolidinium trifluorotris(perfluoroethyl)phosphate
• Measurements of activity coefficients at infinite dilution for organic solutes and water in N-hexylisoquinolinium thiocyanate, [HiQuin][SCN] using GLC
• Measurement of critical temperatures and critical pressures for binary mixtures of methyl tert-butyl ether (MTBE) + alcohol and MTBE + alkane
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-hydroxyethyl)- 3-methylimidazolium trifluorotris(perfluoroethyl)phosphate
• Infinite dilution activity coefficients of volatile organic compounds in two ionic liquids composed of the tris(pentafluoroethyl) trifluorophosphate ([FAP]) anion and a functionalized cation
• Experimental and theoretical excess molar enthalpies of ternary and binary mixtures containing 2-Methoxy-2-Methylpropane, 1-propanol, heptane
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tricyanomethanide
• Thermodynamics and activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylmorpholinium tricyanomethanide
• The study of activity coefficients at infinite dilution for organic solutes and water in 1-butyl-4-methylpyridinium dicyanamide, [B4MPy][DCA] using GLC
• Contribution to study of the thermodynamics properties of mixtures containing 2-methoxy-2-methylpropane, alkanol, alkane
• Measurement and correlation of critical properties for binary mixtures and ternary mixtures containing gasoline additives
• Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
• Solubility and solution thermodynamics of sorbic acid in eight pure organic solvents
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(3-hydroxypropyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
• Activity coefficients at infinite dilution for organic solutes and water in 1-ethyl-1-methylpyrrolidinium lactate
• Activity coefficients at infinite dilution, physicochemical and thermodynamic properties for organic solutes and water in the ionic liquid ethyl-dimethyl-(2-methoxyethyl)ammonium trifluorotris-(perfluoroethyl)phosphate
• Volumetric behavior of the ternary system (methyl tert-butyl ether + methylbenzene + butan-1-ol) and its binary sub-system (methyl tert-butyl ether + butan-1-ol) within the temperature range (298.15 to 328.15) K
• A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
• Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in 1-allyl-3-methylimidazolium bis{(trifluoromethyl)sulfonyl}imide ionic liquid
• Separation of aliphatic from aromatic hydrocarbons and sulphur compounds from fuel based on measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid N,N-diethyl-N-methyl-N-(2-methoxy-ethyl)ammonium bis(trifluoromethylsulfonyl)imide
• Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
• Solubility measurement and correlation of the form A of ibrutinib in organic solvents from 278.15 to 323.15 K
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
• Separation of water/butan-1-ol based on activity coefficients at infinite dilution in 1,3-didecyl-2-methylimidazolium dicyanamide ionic liquid
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on gamma infinity data measurements
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid trihexyl-tetradecyl-phosphonium tricyanomethanide
• Thermodynamic study of molecular interaction-selectivity in separation processes based on limiting activity coefficients
• Liquid-liquid equilibrium for ternary systems of water + 2,2,3,3-tetrafluoro-1-propanol + isopropyl ether/tert-butyl methyl ether at 298.2, 308.2 K
• The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
• Liquid-liquid equilibria for azeotropic mixture of methyl tert-butyl ether and methanol with ionic liquids at different temperatures
• Liquid-liquid equilibrium study for ternary systems of water + propargyl alcohol + solvents at 308.2 K: Measurement and thermodynamic modelling
• Excess molar enthalpies of the ternary mixtures: methyl tert-butyl ether + 3-methylpentane + (n-decane or n-dodecane) at 298.15K
• Isothermal vapor-liquid equilibrium of binary and ternary systems of anisole, hexane, and toluene and ternary system of methyl tert-butyl ether, hexane, and toluene
• sothermal and Isobaric Vapor-Liquid Equilibrium and Excess Molar Enthalpy of the Binary Mixtures of 2-Methoxy-2-methylpropane + 2-Methyl-2-butanol or + 2-Butanol
• Solubility of Amorphous Clopidogrel Hydrogen Sulfate in Different Pure Solvents
• Solubility of Agomelatine Crystal Form I and Form II in Pure Solvents and (Isopropanol + Water) Mixtures
• Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
• Quaternary, Ternary, and Binary LLE Measurements for 2-Methoxy-2-methylpropane + Furfural + Acetic Acid + Water at Temperatures between 298 and 307 K
• Speed of Sound Measurements of 2-Methoxy-2-methylpropane in the Temperature Range of 293.15 and 673.15 K and for Pressures up to 10 MPa
• Liquid-Liquid Equilibria of Ionic Liquids-Water-Acetic Acid Mixtures
• Measurements and Thermodynamic Models for the Separation of 2-Methoxyethanol and Water Azeotropic Mixtures via Different Solvents
• Solid-Liquid Phase Equilibrium and Thermodynamic Properties of Olaparib in Selected Organic Solvents and (Tetrahydrofuran + MTBE, Acetonitrile + Isopropyl Alcohol) Binary Solvent Mixtures
• Solubility Measurement and Thermodynamic Modeling of N-(4-Methylphenyl-Z-3-chloro-2-(phenylthio)propenamide in 12 Pure Solvents at Temperatures Ranging from 278.15 to 318.15 K
• Physicochemical Properties of LiFSI Solutions II: LiFSI with Water, MTBE, and Anisole
• Vapor-Liquid Equilibrium Measurements of Ether Alcohol Blends for Investigation on Reformulated Gas
• Solubility Measurement and Correlation of Probenecid in 12 Pure Organic Solvents and Thermodynamic Properties of Mixing of Solutions
• Measurement and Correlation of the Solubility of Dienogest in Twelve Pure and Water + Methanol Binary Solvents at Temperatures from 273.15 to 318.15 K
• Solubility of Imidazoles in Ethers
• Mixing Properties for the Ternary Mixture Methyl tert-Butyl Ether + 1-Butanol + Decane at 298.15 K
• Vapor-Liquid Equilibria for the Binary Systems of Dimethoxymethane with Some Fuel Oxygenates
• Oxygenated Gasoline Additives: Saturated Heat Capacities between (277 and 355) K
• Excess Molar Volumes and Surface Tensions of Xylene with Isopropyl Ether or Methyl tert-Butyl Ether at 298.15 K
• Solubility of a-Carotene in Binary Solvents Formed by Some Hydrocarbons with tert-Butyl Methyl Ether and with tert-Amyl Methyl Ether
• Liquid-Liquid Equilibrium of MTBE + Ethanol + Water and MTBE + 1-Hexanol + Water over the Temperature Range of 288.15 to 308.15 K
• Experimental and Predicted Excess Molar Enthalpies of the Ternary System tert-Butyl Methyl Ether + 1-Pentanol + Decane at 298.15 K
• Vapor-Liquid Equilibrium Measurements of MTBE and TAME with Toluene
• Measurement of Activity Coefficients at Infinite Dilution of Benzene, Toluene, Ethanol, Esters, Ketones, and Ethers at Various Temperatures in Water Using the Dilutor Technique
• Vapor-Liquid Equilibria for the Ternary Systems of Methyl tert-Butyl Ether + Methanol + Methylcyclohexane and Methyl tert-Butyl Ether + Methanol + n-Heptane and Constituent Binary Systems at 313.15 K
• Liquid-Liquid Equilibria for the Ternary Systems Water + 3-Methyl-2-cyclopentenone with Ethyl Acetate or Methyl tert-Butyl Ether at 293.2 K
• Distribution of Butyric Acid between Water and Several Solvents
• Densities and Viscosities for the Ternary Systems of Methyl tert-Butyl Ether + Methanol + Benzene and Methyl tert-Butyl Ether + Methanol + Toluene and Their Sub-binary Systems at 298.15 K
• Surface Tension of Dimethoxymethane and Methyl tert-Butyl Ether
• Phase Equilibrium Properties of Binary and Ternary Mixtures Containing 1,1-Dimethylethyl Methyl Ether, 1-Propanol, and Hexane at T ) 313.15 K
• Liquid-Liquid Equilibria of the Ternary System Water + Acetic Acid + Methyl tert-Butyl Ether
• Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Butyl-3-methyl-pyridinium Trifluoromethanesulfonate
• Solubility of Artemisinin in Different Single and Binary Solvent Mixtures Between (284.15 and 323.15) K and NRTL Interaction Parameters
• Determination of Activity Coefficients at Infinite Dilution of 35 Solutes in the Ionic Liquid, 1-Butyl-3-methylimidazolium Tosylate, Using Gas-Liquid Chromatography
• Density, Viscosity, Vapor-Liquid Equilibrium, and Excess Molar Enthalpy of [Chloroform + Methyl tert-Butyl Ether]
• Measurements of Activity Coefficients at Infinite Dilution for Organic Solutes and Water in the Ionic Liquid 1-Butyl-1-methylpiperydinium Thiocyanate
• Interactions of Volatile Organic Compounds with the Ionic Liquid 1-Butyl-1-methylpyrrolidinium Dicyanamide
• Excess Molar Enthalpies of Ternary and Binary Mixtures Containing 2-Methoxy-2-Methylpropane, Ethanol, and Nonane
• Excess Volumes of Ternary Mixtures 2,2,4-Trimethylpentane + Diisopropyl Ether or Methyl tert-Butyl Ether + Methanol, Ethanol, or 1-Propanol at 298.15 K
• Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
• Liquid Liquid Equilibria for the Ternary System 2-Methoxy-2-methylpropane + Phenol + Water
• Measurements of Liquid Liquid Equilibria for the Quaternary System 2-Methoxy-2-methylpropane + Phenol + Hydroquinone + Water at 313.15 K
• Thermal Diffusivity of 2-Methoxy-2-methylpropane at Temperatures from (303.15 to 493.15) K and Pressures from (1.5 to 10) MPa
• Experimental Determination and Correlation of Liquid Liquid Equilibria for the Ternary System 2-Methoxy-2-methylpropane + o-Cresol + Water at 298.15 K and 313.15 K
• Densities and Viscosities of MTBE + Heptane or Octane at p ) 0.1 MPa from (273.15 to 363.15) K
• Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
• Phase Equilibria of (1-Ethyl-3-methylimidazolium Ethylsulfate + Hydrocarbon, + Ketone, and + Ether) Binary Systems
• Excess Enthalpy, Density, and Speed of Sound for the Ternary Mixture Methyl tert-Butyl Ether (1) + Butan-1-ol (2) + Octane (3)
• Determination of Temperature-Dependent Henry s Law Constant of Four Oxygenated Solutes in Water Using Headspace Solid-Phase Microextraction Technique
• Measurement and Correlation of Liquid-Liquid Equilibrium Data for Water + Acetic Acid + Methyl tert-Butyl Ether + NaCl
• Excess Molar Enthalpies of Ternary and Binary Mixtures Containing 2-Methoxy-2-methylpropane, 1-Propanol, and Nonane
• Isobaric Vapor-Liquid Equilibria at 101.32 kPa and Densities, Speeds of Sound, and Refractive Indices at 298.15 K for MTBE or DIPE or TAME + 1-Propanol Binary Systems
• Vapor-Liquid Equilibria and Interfacial Tensions of the System Ethanol + 2-Methoxy-2-methylpropane
• Mixing Properties for Binary Liquid Mixtures of Methyl tert-Butyl Ether with Propylamine and Dipropylamine at Temperatures from (288.15 to 308.15) K
• Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Hexyl-3-methylimidazolium Thiocyanate
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• NCMS SOLV-DB
• The Yaws Handbook of Vapor Pressure

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