Chemical Properties of Methyl valerate (CAS 624-24-8)

InChI

InChI=1S/C6H12O2/c1-3-4-5-6(7)8-2/h3-5H2,1-2H3

InChI Key

HNBDRPTVWVGKBR-UHFFFAOYSA-N

Formula

C6H12O2

SMILES

CCCCC(=O)OC

Molecular Weight¹

116.16

CAS

624-24-8

Other Names

• CH3(CH2)3COOCH3
• Methyl ester of pentanoic acid
• Methyl n-valerate
• Methyl pentanoate
• Methyl valerianate
• Pentanoic acid, methyl ester
• Propyl propanoate
• Valeric acid, methyl ester
• n-Valeric acid methyl ester
• valeric acid methyl ester

• ω : Acentric Factor.
• 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).
• 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).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_c : Critical density (kg/m³).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• λ : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• V_c : Critical Volume (m³/kmol).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.4362		Relay (1.0) Calculated Property
ΔcH°liquid	[-3561.70; -3548.00]	kJ/mol
ΔcH°liquid	-3561.70 ± 0.60	kJ/mol	NIST
ΔcH°liquid	-3548.00	kJ/mol	NIST
ΔfG°	-234.28	kJ/mol	Joback Calculated Property
ΔfH°gas	[-485.00; -472.00]	kJ/mol
ΔfH°gas	-472.00 ± 2.00	kJ/mol	NIST
ΔfH°gas	-485.00 ± 2.00	kJ/mol	NIST
ΔfH°liquid	[-527.00; -514.20]	kJ/mol
ΔfH°liquid	-514.20 ± 7.10	kJ/mol	NIST
ΔfH°liquid	-527.00	kJ/mol	NIST
ΔfusH°	14.08	kJ/mol	Joback Calculated Property
ΔvapH°	41.46	kJ/mol	Relay (1.0) Calculated Property
IE	10.40 ± 0.20	eV	NIST
log10WS	[-1.36; -1.34]
log10WS	-1.36		Aq. Solubility Prediction
log10WS	-1.34		Estimated Solubility
logPoct/wat	1.350		Crippen Calculated Property
McVol	102.840	ml/mol	McGowan Calculated Property
Pc	3190.00 ± 202.65	kPa	NIST
ρc	278.78 ± 19.75	kg/m3	NIST
Inp	[784.00; 852.00]
Inp	822.80		NIST
Inp	821.90		NIST
Inp	821.20		NIST
Inp	794.00		NIST
Inp	802.00		NIST
Inp	806.00		NIST
Inp	816.00		NIST
Inp	807.00		NIST
Inp	812.00		NIST
Inp	814.00		NIST
Inp	800.00		NIST
Inp	806.00		NIST
Inp	810.00		NIST
Inp	807.00		NIST
Inp	823.00		NIST
Inp	823.00		NIST
Inp	823.00		NIST
Inp	825.00		NIST
Inp	804.00		NIST
Inp	808.80		NIST
Inp	807.00		NIST
Inp	Outlier 852.00		NIST
Inp	808.00		NIST
Inp	821.00		NIST
Inp	825.00		NIST
Inp	808.00		NIST
Inp	823.00		NIST
Inp	809.00		NIST
Inp	821.00		NIST
Inp	829.10		NIST
Inp	823.00		NIST
Inp	823.00		NIST
Inp	811.00		NIST
Inp	806.00		NIST
Inp	810.00		NIST
Inp	810.00		NIST
Inp	807.00		NIST
Inp	806.00		NIST
Inp	Outlier 784.00		NIST
Inp	830.00		NIST
Inp	807.00		NIST
Inp	806.00		NIST
Inp	808.00		NIST
Inp	823.00		NIST
Inp	808.80		NIST
Inp	821.00		NIST
Inp	822.80		NIST
Inp	806.00		NIST
Inp	800.00		NIST
Inp	830.00		NIST
I	[1075.00; 1123.00]
I	1083.00		NIST
I	Outlier 1123.00		NIST
I	1081.00		NIST
I	1085.00		NIST
I	1089.00		NIST
I	1075.00		NIST
I	1086.00		NIST
I	1096.00		NIST
I	1090.00		NIST
I	1084.00		NIST
I	1090.00		NIST
I	1095.00		NIST
I	1082.00		NIST
I	1087.00		NIST
I	1086.00		NIST
I	1081.00		NIST
I	1085.00		NIST
I	1076.00		NIST
I	1082.00		NIST
I	1083.00		NIST
I	1076.00		NIST
I	Outlier 1109.00		NIST
I	1083.00		NIST
Tboil	400.48	K	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Tc	[556.70; 566.90]	K
Tc	556.70 ± 20.00	K	NIST
Tc	566.90 ± 20.00	K	NIST
Tfus	182.50 ± 0.05	K	NIST
Vc	0.385	m3/kmol	Relay (1.0) Calculated Property

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[199.87; 254.27]	J/mol×K	[412.97; 590.55]
Cp,gas	199.87	J/mol×K	412.97	Joback Calculated Property
Cp,gas	209.71	J/mol×K	442.57	Joback Calculated Property
Cp,gas	219.25	J/mol×K	472.16	Joback Calculated Property
Cp,gas	228.47	J/mol×K	501.76	Joback Calculated Property
Cp,gas	237.38	J/mol×K	531.36	Joback Calculated Property
Cp,gas	245.98	J/mol×K	560.96	Joback Calculated Property
Cp,gas	254.27	J/mol×K	590.55	Joback Calculated Property
Cp,liquid	[226.11; 229.30]	J/mol×K	[298.15; 298.15]
Cp,liquid	226.11	J/mol×K	298.15	NIST
Cp,liquid	229.30	J/mol×K	298.15	NIST
η	[0.0005510; 0.0008160]	Pa×s	[283.15; 313.15]
η	0.0008160	Pa×s	283.15	A Study on Properties Derived from Densities and Viscosities for the Ternary Systems (Methyl Pentanoate or Methyl Heptanoate) + n-Octane + 1-Hexanol and their Binary Subsystems at Various Temperatures.
η	0.0007120	Pa×s	293.15	A Study on Properties Derived from Densities and Viscosities for the Ternary Systems (Methyl Pentanoate or Methyl Heptanoate) + n-Octane + 1-Hexanol and their Binary Subsystems at Various Temperatures.
η	0.0006610	Pa×s	298.15	A Study on Properties Derived from Densities and Viscosities for the Ternary Systems (Methyl Pentanoate or Methyl Heptanoate) + n-Octane + 1-Hexanol and their Binary Subsystems at Various Temperatures.
η	0.0006230	Pa×s	303.15	A Study on Properties Derived from Densities and Viscosities for the Ternary Systems (Methyl Pentanoate or Methyl Heptanoate) + n-Octane + 1-Hexanol and their Binary Subsystems at Various Temperatures.
η	0.0005510	Pa×s	313.15	A Study on Properties Derived from Densities and Viscosities for the Ternary Systems (Methyl Pentanoate or Methyl Heptanoate) + n-Octane + 1-Hexanol and their Binary Subsystems at Various Temperatures.
ΔvapH	[39.20; 44.40]	kJ/mol	[350.00; 414.00]
ΔvapH	41.30	kJ/mol	350.00	NIST
ΔvapH	42.50	kJ/mol	354.00	NIST
ΔvapH	44.10 ± 0.10	kJ/mol	382.50	NIST
ΔvapH	39.20	kJ/mol	390.50	NIST
ΔvapH	44.40	kJ/mol	414.00	NIST
Pvap	[0.34; 101.30]	kPa	[274.90; 400.48]
Pvap	0.34	kPa	274.90	Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap	0.34	kPa	275.20	Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap	0.42	kPa	278.20	Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap	0.46	kPa	279.40	Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap	0.52	kPa	281.20	Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap	0.56	kPa	282.60	Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap	0.64	kPa	284.20	Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap	0.60	kPa	284.30	Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap	0.62	kPa	284.50	Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap	0.69	kPa	285.50	Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap	0.75	kPa	287.40	Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap	0.79	kPa	288.40	Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap	0.78	kPa	288.40	Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap	0.82	kPa	288.50	Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap	0.83	kPa	288.70	Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap	0.87	kPa	289.20	Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap	0.93	kPa	290.30	Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap	1.03	kPa	292.40	Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap	1.09	kPa	293.30	Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap	1.13	kPa	293.40	Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap	1.23	kPa	294.50	Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap	1.33	kPa	296.20	Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap	1.51	kPa	297.50	Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap	1.52	kPa	298.30	Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap	1.61	kPa	299.20	Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap	1.58	kPa	299.20	Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap	1.97	kPa	302.20	Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap	1.94	kPa	302.20	Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap	2.27	kPa	305.20	Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap	2.65	kPa	308.20	Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap	3.11	kPa	311.20	Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
Pvap	29.41	kPa	361.82	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap	35.06	kPa	366.70	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap	40.47	kPa	370.86	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap	45.81	kPa	374.53	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap	52.83	kPa	378.84	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap	59.35	kPa	382.55	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap	60.00	kPa	383.29	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap	69.02	kPa	387.18	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap	77.71	kPa	391.14	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap	88.17	kPa	395.42	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap	95.08	kPa	398.03	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap	100.40	kPa	400.07	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap	101.30	kPa	400.48	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
n0	[1.39470; 1.39710]		[298.15; 298.15]
n0	1.39500		298.15	Thermodynamic study of (alkyl esters + alpha,omega-alkyl dihalides) IV: Hex and Vex for 25 binary mixtures {xC(u-1)H(2u-1)CO2CH3 + (1-x)alpha,omega-BrCH2(CH2)(v-2)CH2Br}, where u = 1 to 5, alpha = 1 and v = omega = 2 to 6
n0	1.39520		298.15	Mixing thermodynamic properties of ester-containing solutions: A study on the ternary (methyl alkanoate (pentanoate and methanoate) + methanol) and the corresponding binaries. New contributions to the (ester + ester) interactions
n0	1.39680		298.15	A Study on Alkane + Ester + Ester Systems. Physicochemical Behavior of Binaries and Ternaries of Octane or Iso-octane with Methyl Esters (Ethanoate, Butanoate, Pentanoate)
n0	1.39470		298.15	Isobaric Vapor-Liquid Equilibria and Excess Properties for the Binary Systems of Methyl Esters + Heptane
n0	1.39710		298.15	Vapor-Liquid Equilibrium Data for the Binary Methyl Esters (Butyrate, Pentanoate, and Hexanoate) (1) + Acetonitrile (2) Systems at 93.32 kPa
n0	1.39710		298.15	Vapor-Liquid Equilibrium Data for the Binary Methyl Esters (Butyrate, Pentanoate, and Hexanoate) (1) + Propanenitrile (2) Systems at 93.32 kPa
ρl	885.66	kg/m3	298.15	Densities and interfacial tensions for fatty acid methyl esters (from methyl formate to methyl heptanoate) + water demixed mixtures at atmospheric pressure conditions
λ	[0.12; 0.14]	W/m×K	[285.55; 362.16]
λ	0.14	W/m×K	285.55	Experimental investigations on the liquid thermal conductivity of five saturated fatty acid methyl esters components of biodiesel
λ	0.14	W/m×K	290.39	Experimental investigations on the liquid thermal conductivity of five saturated fatty acid methyl esters components of biodiesel
λ	0.14	W/m×K	295.51	Experimental investigations on the liquid thermal conductivity of five saturated fatty acid methyl esters components of biodiesel
λ	0.14	W/m×K	298.99	Experimental investigations on the liquid thermal conductivity of five saturated fatty acid methyl esters components of biodiesel
λ	0.14	W/m×K	305.50	Experimental investigations on the liquid thermal conductivity of five saturated fatty acid methyl esters components of biodiesel
λ	0.13	W/m×K	312.35	Experimental investigations on the liquid thermal conductivity of five saturated fatty acid methyl esters components of biodiesel
λ	0.13	W/m×K	320.42	Experimental investigations on the liquid thermal conductivity of five saturated fatty acid methyl esters components of biodiesel
λ	0.13	W/m×K	327.35	Experimental investigations on the liquid thermal conductivity of five saturated fatty acid methyl esters components of biodiesel
λ	0.13	W/m×K	333.50	Experimental investigations on the liquid thermal conductivity of five saturated fatty acid methyl esters components of biodiesel
λ	0.12	W/m×K	340.41	Experimental investigations on the liquid thermal conductivity of five saturated fatty acid methyl esters components of biodiesel
λ	0.12	W/m×K	348.36	Experimental investigations on the liquid thermal conductivity of five saturated fatty acid methyl esters components of biodiesel
λ	0.12	W/m×K	355.39	Experimental investigations on the liquid thermal conductivity of five saturated fatty acid methyl esters components of biodiesel
λ	0.12	W/m×K	362.16	Experimental investigations on the liquid thermal conductivity of five saturated fatty acid methyl esters components of biodiesel

Datasets

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.15	100.00	890.18
293.15	1000.00	890.39
293.15	3000.00	892.23
293.15	5000.00	893.59
293.15	10000.00	897.77
293.15	15000.00	901.59
293.15	20000.00	905.28
293.15	25000.00	908.91
293.15	30000.00	912.4
293.15	35000.00	915.63
293.15	40000.00	918.78
293.15	50000.00	925.12
293.15	60000.00	930.63
303.15	100.00	879.57
303.15	1000.00	880.52
303.15	3000.00	882.29
303.15	5000.00	884.05
303.15	10000.00	888.3
303.15	15000.00	892.37
303.15	20000.00	896.14
303.15	25000.00	899.89
303.15	30000.00	903.55
303.15	35000.00	906.97
303.15	40000.00	910.27
303.15	50000.00	916.73
303.15	60000.00	922.74
313.15	100.00	869.49
313.15	1000.00	869.89
313.15	3000.00	871.87
313.15	5000.00	873.76
313.15	10000.00	878.33
313.15	15000.00	882.44
313.15	20000.00	886.62
313.15	25000.00	890.61
313.15	30000.00	894.38
313.15	35000.00	898.09
313.15	40000.00	901.45
313.15	50000.00	908.24
313.15	60000.00	914.32
323.15	100.00	858.83
323.15	1000.00	859.81
323.15	3000.00	861.81
323.15	5000.00	863.85
323.15	10000.00	868.67
323.15	15000.00	873.18
323.15	20000.00	877.67
323.15	25000.00	881.64
323.15	30000.00	885.65
323.15	35000.00	889.44
323.15	40000.00	893.13
323.15	50000.00	900.12
323.15	60000.00	906.77
333.15	100.00	848.52
333.15	1000.00	849.45
333.15	3000.00	851.71
333.15	5000.00	853.79
333.15	10000.00	858.86
333.15	15000.00	863.66
333.15	20000.00	868.26
333.15	25000.00	872.72
333.15	30000.00	876.79
333.15	35000.00	880.79
333.15	40000.00	884.78
333.15	50000.00	892.02
333.15	60000.00	898.8
343.15	100.00	837.8
343.15	1000.00	839.04
343.15	3000.00	841.41
343.15	5000.00	843.76
343.15	10000.00	849.05
343.15	15000.00	854.23
343.15	20000.00	859.25
343.15	25000.00	863.69
343.15	30000.00	868.17
343.15	35000.00	872.41
343.15	40000.00	876.28
343.15	50000.00	884.03
343.15	60000.00	890.84
353.15	100.00	827.35
353.15	1000.00	828.43
353.15	3000.00	831.13
353.15	5000.00	833.48
353.15	10000.00	839.27
353.15	15000.00	844.84
353.15	20000.00	849.86
353.15	25000.00	854.79
353.15	30000.00	859.45
353.15	35000.00	863.9
353.15	40000.00	868.0
353.15	50000.00	875.94
353.15	60000.00	883.37
363.15	100.00	816.63
363.15	1000.00	817.89
363.15	3000.00	820.7
363.15	5000.00	823.32
363.15	10000.00	829.23
363.15	15000.00	835.46
363.15	20000.00	840.59
363.15	25000.00	845.61
363.15	30000.00	850.57
363.15	35000.00	855.31
363.15	40000.00	859.8
363.15	50000.00	868.09
363.15	60000.00	875.9
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.64]	kPa	[297.44; 438.38]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.40423e+01
Coefficient B			-3.36903e+03
Coefficient C			-5.25030e+01
Temperature range, min.			297.44
Temperature range, max.			438.38
Pvap	1.33	kPa	297.44	Calculated Property
Pvap	3.05	kPa	313.10	Calculated Property
Pvap	6.34	kPa	328.76	Calculated Property
Pvap	12.20	kPa	344.42	Calculated Property
Pvap	21.95	kPa	360.08	Calculated Property
Pvap	37.32	kPa	375.74	Calculated Property
Pvap	60.41	kPa	391.40	Calculated Property
Pvap	93.71	kPa	407.06	Calculated Property
Pvap	140.07	kPa	422.72	Calculated Property
Pvap	202.64	kPa	438.38	Calculated Property
Pvap	[6.52; 2812.70]	kPa	[318.15; 575.15]	KDB Vapor Pressure Data
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			1.06981e+02
Coefficient B			-8.88364e+03
Coefficient C			-1.35161e+01
Coefficient D			6.94116e-06
Temperature range, min.			318.15
Temperature range, max.			575.15
Pvap	6.52	kPa	318.15	Calculated Property
Pvap	23.20	kPa	346.71	Calculated Property
Pvap	64.54	kPa	375.26	Calculated Property
Pvap	149.08	kPa	403.82	Calculated Property
Pvap	298.76	kPa	432.37	Calculated Property
Pvap	536.55	kPa	460.93	Calculated Property
Pvap	884.91	kPa	489.48	Calculated Property
Pvap	1365.45	kPa	518.04	Calculated Property
Pvap	2000.03	kPa	546.59	Calculated Property
Pvap	2812.70	kPa	575.15	Calculated Property

Similar Compounds

Find more compounds similar to Methyl valerate.

Mixtures

• Ethane, 1,2-dibromo- + Methyl valerate
• Propane, 1,3-dibromo- + Methyl valerate
• Methyl valerate + Butane, 1,4-dibromo-
• Pentane, 1,5-dibromo- + Methyl valerate
• Hexane, 1,6-dibromo- + Methyl valerate
• Methyl formate + Methyl valerate
• Methyl valerate + Methyl Alcohol
• Methyl formate + Methyl valerate + Methyl Alcohol
• Methyl valerate + Water
• Octane + Methyl valerate
• Methyl valerate + Pentane, 2,2,4-trimethyl-
• Methyl valerate + Acetic acid, methyl ester
• Octane + Methyl valerate + Acetic acid, methyl ester
• Methyl valerate + Pentane, 2,2,4-trimethyl- + Acetic acid, methyl ester
• Methyl valerate + Heptane
• Methyl valerate + 1-Hexanol
• Octane + Methyl valerate + 1-Hexanol
• Acetonitrile + Methyl valerate
• Propanenitrile + Methyl valerate

Sources

• KDB Vapor Pressure Data
• Cheméo Relay (1.0)
• Crippen Method
• Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
• High-pressure liquid densities of fatty acid methyl esters: Measurement and prediction with the PC-SAFT equation of state
• Thermodynamic study of (alkyl esters + alpha,omega-alkyl dihalides) IV: Hex and Vex for 25 binary mixtures {xC(u-1)H(2u-1)CO2CH3 + (1-x)alpha,omega-BrCH2(CH2)(v-2)CH2Br}, where u = 1 to 5, alpha = 1 and v = omega = 2 to 6
• Mixing thermodynamic properties of ester-containing solutions: A study on the ternary (methyl alkanoate (pentanoate and methanoate) + methanol) and the corresponding binaries. New contributions to the (ester + ester) interactions
• Densities and interfacial tensions for fatty acid methyl esters (from methyl formate to methyl heptanoate) + water demixed mixtures at atmospheric pressure conditions
• Experimental investigations on the liquid thermal conductivity of five saturated fatty acid methyl esters components of biodiesel
• A Study on Alkane + Ester + Ester Systems. Physicochemical Behavior of Binaries and Ternaries of Octane or Iso-octane with Methyl Esters (Ethanoate, Butanoate, Pentanoate)
• Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
• Isobaric Vapor-Liquid Equilibria and Excess Properties for the Binary Systems of Methyl Esters + Heptane
• A Study on Properties Derived from Densities and Viscosities for the Ternary Systems (Methyl Pentanoate or Methyl Heptanoate) + n-Octane + 1-Hexanol and their Binary Subsystems at Various Temperatures.
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 8. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 9. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in Trimethyl-butylammonium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography and Static Method
• Vapor-Liquid Equilibrium Data for the Binary Methyl Esters (Butyrate, Pentanoate, and Hexanoate) (1) + Acetonitrile (2) Systems at 93.32 kPa
• Experimental Study of Thermodynamic Properties of Mixtures Containing Ionic Liquid 1-Ethyl-3-methylimidazolium Ethyl Sulfate Using Gas-Liquid Chromatography and Transpiration Method
• Vapor-Liquid Equilibrium Data for the Binary Methyl Esters (Butyrate, Pentanoate, and Hexanoate) (1) + Propanenitrile (2) Systems at 93.32 kPa
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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Outlier This icon means that the value is more than 2 standard deviations away from the property mean.