Chemical Properties of Butane, 2-ethoxy-2-methyl- (CAS 919-94-8)

InChI

InChI=1S/C7H16O/c1-5-7(3,4)8-6-2/h5-6H2,1-4H3

InChI Key

KFRVYYGHSPLXSZ-UHFFFAOYSA-N

Formula

C7H16O

SMILES

CCOC(C)(C)CC

Molecular Weight¹

116.20

CAS

919-94-8

Other Names

• 1,1-dimethylpropyl ethyl ether
• 2-Ethoxy-2-methylbutane
• 2-Ethyl-2-ethoxypropane
• Ethyl 1,1-dimethylpropyl ether
• Ethyl tert-amyl ether
• ether, 1,1-dimethylpropyl ethyl
• ethyl tert-pentyl ether

• ω : Acentric Factor.
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• 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_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• 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.
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• λ : Gas thermal conductivity (W/m×K).
• λ : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• U_Qi : UNIQUAC Qi Parameter.
• U_Ri : UNIQUAC Ri Parameter.
• V_c : Critical Volume (m³/kmol).
• Z_c : Critical Compressibility.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.3382		ChemSep v8.3 pure component data
μ	1.54	debye	ChemSep v8.3 pure component data
ΔfG°	-109.40	kJ/mol	ChemSep v8.3 pure component data
ΔfH°gas	-332.40	kJ/mol	ChemSep v8.3 pure component data
ΔfH°liquid	-379.80 ± 1.40	kJ/mol	NIST
ΔfusH°	7.66	kJ/mol	Joback Calculated Property
ΔvapH°	[38.20; 39.20]	kJ/mol
ΔvapH°	39.20 ± 0.40	kJ/mol	NIST
ΔvapH°	38.20 ± 0.20	kJ/mol	NIST
IE	9.27	eV	Relay (1.0) Calculated Property
logPoct/wat	2.212		Crippen Calculated Property
McVol	115.360	ml/mol	McGowan Calculated Property
Pc	2740.00	kPa	ChemSep v8.3 pure component data
Ptriple	7.30e-04	kPa	ChemSep v8.3 pure component data
Inp	[721.00; 730.00]
Inp	726.00		NIST
Inp	730.00		NIST
Inp	721.00		NIST
Tboil	[374.15; 375.20]	K
Tboil	374.57	K	Isobaric vapor liquid equilibria for systems composed by 2-ethoxy-2-methylbutane, methanol or ethanol and water at 101.32 kPa
Tboil	374.15	K	ChemSep v8.3 pure component data
Tboil	375.20	K	NIST
Tc	544.00	K	ChemSep v8.3 pure component data
Tfus	190.00	K	ChemSep v8.3 pure component data
Ttriple	190.00	K	ChemSep v8.3 pure component data
UQi	4.71		ChemSep v8.3 pure component data
URi	5.42		ChemSep v8.3 pure component data
Vc	0.435	m3/kmol	ChemSep v8.3 pure component data
Zc	0.2730000		ChemSep v8.3 pure component data
Zra	0.27		ChemSep v8.3 pure component data

Cheméo can also estimate Log10 of Water solubility in mol/l for this compound, but it falls outside the models' validated range, so it is not shown here. Open the prediction tool to compute it on demand.

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	243.00	J/mol×K	298.00	NIST
ΔvapH	[35.60; 35.70]	kJ/mol	[346.00; 347.00]
ΔvapH	35.70	kJ/mol	346.00	NIST
ΔvapH	35.60	kJ/mol	347.00	NIST
Pvap	[1.41; 98.94]	kPa	[274.20; 373.71]
Pvap	1.41	kPa	274.20	Determination of Ambient Temperature Vapor Pressures and Vaporization Enthalpies of Branched Ethers
Pvap	1.61	kPa	276.20	Determination of Ambient Temperature Vapor Pressures and Vaporization Enthalpies of Branched Ethers
Pvap	1.82	kPa	278.20	Determination of Ambient Temperature Vapor Pressures and Vaporization Enthalpies of Branched Ethers
Pvap	2.06	kPa	280.20	Determination of Ambient Temperature Vapor Pressures and Vaporization Enthalpies of Branched Ethers
Pvap	2.34	kPa	282.20	Determination of Ambient Temperature Vapor Pressures and Vaporization Enthalpies of Branched Ethers
Pvap	2.67	kPa	284.20	Determination of Ambient Temperature Vapor Pressures and Vaporization Enthalpies of Branched Ethers
Pvap	3.21	kPa	287.20	Determination of Ambient Temperature Vapor Pressures and Vaporization Enthalpies of Branched Ethers
Pvap	3.74	kPa	290.20	Determination of Ambient Temperature Vapor Pressures and Vaporization Enthalpies of Branched Ethers
Pvap	4.44	kPa	293.20	Determination of Ambient Temperature Vapor Pressures and Vaporization Enthalpies of Branched Ethers
Pvap	5.27	kPa	296.20	Determination of Ambient Temperature Vapor Pressures and Vaporization Enthalpies of Branched Ethers
Pvap	6.13	kPa	299.20	Determination of Ambient Temperature Vapor Pressures and Vaporization Enthalpies of Branched Ethers
Pvap	7.19	kPa	302.20	Determination of Ambient Temperature Vapor Pressures and Vaporization Enthalpies of Branched Ethers
Pvap	17.73	kPa	324.31	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing 2-Ethoxy-2-methylpropane or 2-Ethoxy-2-methylbutane and Acetonitrile or Propanenitrile
Pvap	23.98	kPa	331.83	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing 2-Ethoxy-2-methylpropane or 2-Ethoxy-2-methylbutane and Acetonitrile or Propanenitrile
Pvap	36.56	kPa	343.12	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing 2-Ethoxy-2-methylpropane or 2-Ethoxy-2-methylbutane and Acetonitrile or Propanenitrile
Pvap	37.59	kPa	343.83	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing 2-Ethoxy-2-methylpropane or 2-Ethoxy-2-methylbutane and Acetonitrile or Propanenitrile
Pvap	40.29	kPa	345.82	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing 2-Ethoxy-2-methylpropane or 2-Ethoxy-2-methylbutane and Acetonitrile or Propanenitrile
Pvap	45.43	kPa	349.21	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing 2-Ethoxy-2-methylpropane or 2-Ethoxy-2-methylbutane and Acetonitrile or Propanenitrile
Pvap	49.52	kPa	351.71	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing 2-Ethoxy-2-methylpropane or 2-Ethoxy-2-methylbutane and Acetonitrile or Propanenitrile
Pvap	55.54	kPa	355.12	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing 2-Ethoxy-2-methylpropane or 2-Ethoxy-2-methylbutane and Acetonitrile or Propanenitrile
Pvap	59.91	kPa	357.39	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing 2-Ethoxy-2-methylpropane or 2-Ethoxy-2-methylbutane and Acetonitrile or Propanenitrile
Pvap	65.08	kPa	359.96	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing 2-Ethoxy-2-methylpropane or 2-Ethoxy-2-methylbutane and Acetonitrile or Propanenitrile
Pvap	69.66	kPa	362.13	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing 2-Ethoxy-2-methylpropane or 2-Ethoxy-2-methylbutane and Acetonitrile or Propanenitrile
Pvap	71.73	kPa	363.10	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing 2-Ethoxy-2-methylpropane or 2-Ethoxy-2-methylbutane and Acetonitrile or Propanenitrile
Pvap	74.90	kPa	364.42	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing 2-Ethoxy-2-methylpropane or 2-Ethoxy-2-methylbutane and Acetonitrile or Propanenitrile
Pvap	79.62	kPa	366.44	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing 2-Ethoxy-2-methylpropane or 2-Ethoxy-2-methylbutane and Acetonitrile or Propanenitrile
Pvap	81.79	kPa	367.36	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing 2-Ethoxy-2-methylpropane or 2-Ethoxy-2-methylbutane and Acetonitrile or Propanenitrile
Pvap	83.80	kPa	368.16	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing 2-Ethoxy-2-methylpropane or 2-Ethoxy-2-methylbutane and Acetonitrile or Propanenitrile
Pvap	98.94	kPa	373.71	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing 2-Ethoxy-2-methylpropane or 2-Ethoxy-2-methylbutane and Acetonitrile or Propanenitrile
n0	[1.38857; 1.38858]		[298.15; 298.15]
n0	1.38857		298.15	Experimental Determination of Liquid-Liquid Equilibrium Using Ionic Liquids: tert-Amyl Ethyl Ether + Ethanol + 1-Octyl-3-Methylimidazolium Chloride System at 298.15 K
n0	1.38858		298.15	Vapor Liquid Equilibria, Excess Enthalpy, and Excess Volume of Binary Mixtures Containing an Alcohol (1-Butanol, 2-Butanol, or 2-Methyl-2-butanol) and 2-Ethoxy-2-methylbutane

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[138.43; 433.62]	J/mol×K	[190.00; 1200.00]	ChemSep v8.3 pure component data
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K
Coefficient A			1.19820e+02
Coefficient B			-6.47930e+02
Coefficient C			6.34324e+00
Coefficient D			-4.89300e-05
Coefficient E			2.89510e-09
Comment			ChemSep eq 16, IdealGasHeatCapacityCp
Temperature range, min.			190.00
Temperature range, max.			1200.00
Cp,gas	138.43	J/mol×K	190.00	Calculated Property
Cp,gas	185.50	J/mol×K	302.22	Calculated Property
Cp,gas	236.58	J/mol×K	414.44	Calculated Property
Cp,gas	281.89	J/mol×K	526.67	Calculated Property
Cp,gas	319.96	J/mol×K	638.89	Calculated Property
Cp,gas	351.53	J/mol×K	751.11	Calculated Property
Cp,gas	377.74	J/mol×K	863.33	Calculated Property
Cp,gas	399.63	J/mol×K	975.56	Calculated Property
Cp,gas	418.03	J/mol×K	1087.78	Calculated Property
Cp,gas	433.62	J/mol×K	1200.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[222.79; 383.09]	J/mol×K	[272.00; 520.00]	ChemSep v8.3 pure component data
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K
Coefficient A			-7.96040e+01
Coefficient B			-3.98250e+02
Coefficient C			8.48424e+00
Coefficient D			-6.75050e-03
Coefficient E			7.13370e-06
Comment			ChemSep eq 16, LiquidHeatCapacityCp
Temperature range, min.			272.00
Temperature range, max.			520.00
Cp,liquid	222.79	J/mol×K	272.00	Calculated Property
Cp,liquid	241.82	J/mol×K	299.56	Calculated Property
Cp,liquid	258.02	J/mol×K	327.11	Calculated Property
Cp,liquid	272.71	J/mol×K	354.67	Calculated Property
Cp,liquid	287.01	J/mol×K	382.22	Calculated Property
Cp,liquid	301.87	J/mol×K	409.78	Calculated Property
Cp,liquid	318.13	J/mol×K	437.33	Calculated Property
Cp,liquid	336.57	J/mol×K	464.89	Calculated Property
Cp,liquid	357.95	J/mol×K	492.44	Calculated Property
Cp,liquid	383.09	J/mol×K	520.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0040155; 0.0002110]	Pa×s	[190.00; 374.57]	ChemSep v8.3 pure component data
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-1.14350e+01
Coefficient B			1.13430e+03
Coefficient C			-1.02000e-02
Coefficient D			2.55200e-08
Coefficient E			2.00000e+00
Comment			ChemSep eq 101, LiquidViscosity
Temperature range, min.			190.00
Temperature range, max.			374.57
η	0.0040155	Pa×s	190.00	Calculated Property
η	0.0022428	Pa×s	210.51	Calculated Property
η	0.0013891	Pa×s	231.02	Calculated Property
η	0.0009303	Pa×s	251.52	Calculated Property
η	0.0006618	Pa×s	272.03	Calculated Property
η	0.0004938	Pa×s	292.54	Calculated Property
η	0.0003829	Pa×s	313.05	Calculated Property
η	0.0003064	Pa×s	333.55	Calculated Property
η	0.0002515	Pa×s	354.06	Calculated Property
η	0.0002110	Pa×s	374.57	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[40.63; 12.25]	kJ/mol	[190.00; 527.26]	ChemSep v8.3 pure component data
Equation			Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K
Coefficient A			6.44805e+01
Coefficient B			2.47576e+00
Coefficient C			-5.83086e+00
Coefficient D			5.95818e+00
Coefficient E			-2.13554e+00
Critical temperature, Tc (K)			5.44000e+02
Comment			ChemSep eq 106, HeatOfVaporization
Temperature range, min.			190.00
Temperature range, max.			527.26
ΔvapH	40.63	kJ/mol	190.00	Calculated Property
ΔvapH	39.11	kJ/mol	227.47	Calculated Property
ΔvapH	37.74	kJ/mol	264.95	Calculated Property
ΔvapH	36.27	kJ/mol	302.42	Calculated Property
ΔvapH	34.51	kJ/mol	339.89	Calculated Property
ΔvapH	32.27	kJ/mol	377.37	Calculated Property
ΔvapH	29.36	kJ/mol	414.84	Calculated Property
ΔvapH	25.58	kJ/mol	452.31	Calculated Property
ΔvapH	20.49	kJ/mol	489.79	Calculated Property
ΔvapH	12.25	kJ/mol	527.26	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.63]	kPa	[280.06; 398.08]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.53048e+01
Coefficient B			-3.52566e+03
Coefficient C			-4.52800e+01
Temperature range, min.			280.06
Temperature range, max.			398.08
Pvap	1.33	kPa	280.06	Calculated Property
Pvap	2.95	kPa	293.17	Calculated Property
Pvap	6.03	kPa	306.29	Calculated Property
Pvap	11.51	kPa	319.40	Calculated Property
Pvap	20.70	kPa	332.51	Calculated Property
Pvap	35.38	kPa	345.63	Calculated Property
Pvap	57.81	kPa	358.74	Calculated Property
Pvap	90.82	kPa	371.85	Calculated Property
Pvap	137.77	kPa	384.97	Calculated Property
Pvap	202.63	kPa	398.08	Calculated Property
Pvap	[1.76e-03; 3860.79]	kPa	[190.00; 546.00]	ChemSep v8.3 pure component data
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K
Coefficient A			4.02166e+01
Coefficient B			-5.00662e+03
Coefficient C			-3.89210e+00
Coefficient D			5.84380e-06
Coefficient E			2.00000e+00
Comment			ChemSep eq 101, VaporPressure
Temperature range, min.			190.00
Temperature range, max.			546.00
Pvap	1.76e-03	kPa	190.00	Calculated Property
Pvap	0.09	kPa	229.56	Calculated Property
Pvap	1.30	kPa	269.11	Calculated Property
Pvap	9.42	kPa	308.67	Calculated Property
Pvap	43.28	kPa	348.22	Calculated Property
Pvap	146.30	kPa	387.78	Calculated Property
Pvap	399.86	kPa	427.33	Calculated Property
Pvap	939.97	kPa	466.89	Calculated Property
Pvap	1982.00	kPa	506.44	Calculated Property
Pvap	3860.79	kPa	546.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[851.94; 437.55]	kg/m3	[190.00; 527.26]	ChemSep v8.3 pure component data
Equation			Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K
Coefficient A			7.65627e+01
Coefficient B			2.77970e-01
Coefficient C			5.44000e+02
Coefficient D			2.92270e-01
Comment			ChemSep eq 105, LiquidDensity
Temperature range, min.			190.00
Temperature range, max.			527.26
ρl	851.94	kg/m3	190.00	Calculated Property
ρl	821.54	kg/m3	227.47	Calculated Property
ρl	789.71	kg/m3	264.95	Calculated Property
ρl	756.12	kg/m3	302.42	Calculated Property
ρl	720.29	kg/m3	339.89	Calculated Property
ρl	681.52	kg/m3	377.37	Calculated Property
ρl	638.62	kg/m3	414.84	Calculated Property
ρl	589.44	kg/m3	452.31	Calculated Property
ρl	528.93	kg/m3	489.79	Calculated Property
ρl	437.55	kg/m3	527.26	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 6.78e-04]	N/m	[190.00; 527.26]	ChemSep v8.3 pure component data
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K
Coefficient A			-1.20450e-02
Coefficient B			5.12700e+01
Coefficient C			-3.28680e+00
Coefficient D			8.10880e-04
Coefficient E			-5.76360e-06
Comment			ChemSep eq 16, SurfaceTension
Temperature range, min.			190.00
Temperature range, max.			527.26
γ	0.03	N/m	190.00	Calculated Property
γ	0.03	N/m	227.47	Calculated Property
γ	0.03	N/m	264.95	Calculated Property
γ	0.02	N/m	302.42	Calculated Property
γ	0.02	N/m	339.89	Calculated Property
γ	0.01	N/m	377.37	Calculated Property
γ	0.01	N/m	414.84	Calculated Property
γ	0.01	N/m	452.31	Calculated Property
γ	0.00	N/m	489.79	Calculated Property
γ	6.78e-04	N/m	527.26	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λ	[0.01; 0.08]	W/m×K	[190.00; 1000.00]	ChemSep v8.3 pure component data
Equation			Y = A·T^B / (1 + C/T + D/T²) Y is λ in W/m×K, T in K
Coefficient A			1.32950e-04
Coefficient B			9.85040e-01
Coefficient C			4.31520e+02
Coefficient D			3.40600e+04
Comment			ChemSep eq 102, VaporThermalConductivity
Temperature range, min.			190.00
Temperature range, max.			1000.00
λ	0.01	W/m×K	190.00	Calculated Property
λ	0.01	W/m×K	280.00	Calculated Property
λ	0.02	W/m×K	370.00	Calculated Property
λ	0.03	W/m×K	460.00	Calculated Property
λ	0.04	W/m×K	550.00	Calculated Property
λ	0.04	W/m×K	640.00	Calculated Property
λ	0.05	W/m×K	730.00	Calculated Property
λ	0.06	W/m×K	820.00	Calculated Property
λ	0.07	W/m×K	910.00	Calculated Property
λ	0.08	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λ	[0.14; 0.08]	W/m×K	[190.00; 435.20]	ChemSep v8.3 pure component data
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is λ in W/m×K, T in K
Coefficient A			-1.38050e-01
Coefficient B			1.32520e+01
Coefficient C			-1.26180e+00
Coefficient D			-1.81010e-04
Coefficient E			-1.09670e-06
Comment			ChemSep eq 16, LiquidThermalConductivity
Temperature range, min.			190.00
Temperature range, max.			435.20
λ	0.14	W/m×K	190.00	Calculated Property
λ	0.14	W/m×K	217.24	Calculated Property
λ	0.13	W/m×K	244.49	Calculated Property
λ	0.12	W/m×K	271.73	Calculated Property
λ	0.12	W/m×K	298.98	Calculated Property
λ	0.11	W/m×K	326.22	Calculated Property
λ	0.10	W/m×K	353.47	Calculated Property
λ	0.10	W/m×K	380.71	Calculated Property
λ	0.09	W/m×K	407.96	Calculated Property
λ	0.08	W/m×K	435.20	Calculated Property

Similar Compounds

Find more compounds similar to Butane, 2-ethoxy-2-methyl-.

Mixtures

• Butane, 2-ethoxy-2-methyl- + Water
• Butane, 2-ethoxy-2-methyl- + Methyl Alcohol + Water
• Ethanol + Butane, 2-ethoxy-2-methyl- + Water
• 2-Pyrrolidinone, 1-methyl- + Butane, 2-ethoxy-2-methyl-
• Butane, 2-ethoxy-2-methyl- + Methyl Alcohol
• Ethanol + Butane, 2-ethoxy-2-methyl-
• Butane, 2-ethoxy-2-methyl- + 1-Butanol
• Butane, 2-ethoxy-2-methyl- + Amylene hydrate
• Acetonitrile + Butane, 2-ethoxy-2-methyl-
• Propanenitrile + Butane, 2-ethoxy-2-methyl-

Sources

• Cheméo Relay (1.0)
• ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
• Crippen Method
• Crippen Method
• (Solid + liquid) phase equilibria of binary mixtures containing N-methyl-2-pyrrolidinone and ethers at atmospheric pressure
• Isobaric vapor liquid equilibria for systems composed by 2-ethoxy-2-methylbutane, methanol or ethanol and water at 101.32 kPa
• Infinite dilution activity coefficient measurements by inert gas stripping method
• Liquid liquid equilibria for binary systems of tert-amyl ethyl ether (TAEE), isopropyl tert-butyl ether (IPTBE) and di-sec-butyl ether (DSBE) with water and for ternary systems with methanol or ethanol
• Determination of Ambient Temperature Vapor Pressures and Vaporization Enthalpies of Branched Ethers
• Experimental Determination of Liquid-Liquid Equilibrium Using Ionic Liquids: tert-Amyl Ethyl Ether + Ethanol + 1-Octyl-3-Methylimidazolium Chloride System at 298.15 K
• Thermochemistry of Branched Ethers: Experimental Study of Chemical Equilibrium in the Reacting System of tert-Amyl Alkyl Ether Synthesis
• Vapor Liquid Equilibria, Excess Enthalpy, and Excess Volume of Binary Mixtures Containing an Alcohol (1-Butanol, 2-Butanol, or 2-Methyl-2-butanol) and 2-Ethoxy-2-methylbutane
• Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing 2-Ethoxy-2-methylpropane or 2-Ethoxy-2-methylbutane and Acetonitrile or Propanenitrile
• Joback Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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