Chemical Properties of 2-Heptanol (CAS 543-49-7)

InChI

InChI=1S/C7H16O/c1-3-4-5-6-7(2)8/h7-8H,3-6H2,1-2H3

InChI Key

CETWDUZRCINIHU-UHFFFAOYSA-N

Formula

C7H16O

SMILES

CCCCCC(C)O

Molecular Weight¹

116.20

CAS

543-49-7

Other Names

• 1-Methylhexanol
• 2-Heptyl alcohol
• 2-hydroxyheptane
• Amyl methyl carbinol
• CH3(CH2)4CHOHCH3
• Heptan-2-ol
• Heptanol-2
• NSC 2220
• amylmethylcarbinol
• methyl amyl carbinol
• methylpentylcarbinol
• n-Heptan-2-ol
• s-Heptyl alcohol

• ω : Acentric Factor.
• 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).
• T_fus : Normal melting (fusion) point (K).
• V_c : Critical Volume (m³/kmol).
• Z_c : Critical Compressibility.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.6122		Relay (1.0) Calculated Property
Cp,liquid	298.64	J/mol×K	Vapour pressures and heat capacity measurements on the C7 C9 secondary aliphatic alcohols
η	0.0053460	Pa×s	Speeds of sound, isentropic compressibilities, viscosities and excess molar volumes of binary mixtures of methylcyclohexane + 2-alkanols or ethanol at T = 298.15 K
ΔfG°	-131.20	kJ/mol	Joback Calculated Property
ΔfH°gas	-355.40 ± 2.10	kJ/mol	NIST
ΔfH°liquid	-416.90 ± 0.67	kJ/mol	NIST
ΔfusH°	14.45	kJ/mol	Joback Calculated Property
ΔvapH°	62.10 ± 0.40	kJ/mol	NIST
IE	[9.70; 10.24]	eV
IE	9.70 ± 0.03	eV	NIST
IE	10.24	eV	NIST
log10WS	[-1.55; -1.55]
log10WS	-1.55		Aq. Solubility Prediction
log10WS	-1.55		Estimated Solubility
logPoct/wat	1.948		Crippen Calculated Property
McVol	115.360	ml/mol	McGowan Calculated Property
Pc	[3020.00; 3021.00]	kPa
Pc	3021.00	kPa	KDB
Pc	3020.00 ± 20.00	kPa	NIST
Pc	3021.00 ± 20.00	kPa	NIST
Pc	3021.00 ± 20.00	kPa	NIST
ρc	[262.61; 262.61]	kg/m3
ρc	262.61 ± 2.32	kg/m3	NIST
ρc	262.61 ± 19.75	kg/m3	NIST
Inp	[142.33; 924.00]
Inp	882.30		NIST
Inp	888.40		NIST
Inp	890.00		NIST
Inp	868.00		NIST
Inp	877.00		NIST
Inp	889.00		NIST
Inp	888.00		NIST
Inp	886.00		NIST
Inp	887.00		NIST
Inp	886.00		NIST
Inp	882.00		NIST
Inp	888.00		NIST
Inp	904.00		NIST
Inp	883.00		NIST
Inp	883.00		NIST
Inp	888.00		NIST
Inp	888.00		NIST
Inp	921.00		NIST
Inp	924.00		NIST
Inp	904.00		NIST
Inp	877.00		NIST
Inp	882.50		NIST
Inp	884.00		NIST
Inp	885.00		NIST
Inp	887.00		NIST
Inp	887.00		NIST
Inp	901.00		NIST
Inp	900.00		NIST
Inp	900.00		NIST
Inp	888.00		NIST
Inp	901.00		NIST
Inp	901.00		NIST
Inp	884.00		NIST
Inp	886.00		NIST
Inp	886.00		NIST
Inp	897.00		NIST
Inp	896.00		NIST
Inp	892.00		NIST
Inp	901.40		NIST
Inp	905.00		NIST
Inp	906.00		NIST
Inp	908.00		NIST
Inp	886.00		NIST
Inp	900.00		NIST
Inp	900.00		NIST
Inp	900.00		NIST
Inp	903.00		NIST
Inp	903.00		NIST
Inp	896.00		NIST
Inp	888.00		NIST
Inp	900.00		NIST
Inp	900.00		NIST
Inp	900.00		NIST
Inp	911.00		NIST
Inp	885.00		NIST
Inp	890.00		NIST
Inp	887.00		NIST
Inp	915.00		NIST
Inp	905.10		NIST
Inp	906.00		NIST
Inp	893.00		NIST
Inp	903.00		NIST
Inp	880.00		NIST
Inp	880.00		NIST
Inp	880.00		NIST
Inp	881.00		NIST
Inp	888.00		NIST
Inp	888.00		NIST
Inp	898.00		NIST
Inp	919.00		NIST
Inp	881.00		NIST
Inp	881.00		NIST
Inp	894.00		NIST
Inp	881.00		NIST
Inp	889.00		NIST
Inp	901.00		NIST
Inp	908.00		NIST
Inp	889.00		NIST
Inp	894.00		NIST
Inp	875.00		NIST
Inp	889.00		NIST
Inp	906.00		NIST
Inp	918.00		NIST
Inp	879.00		NIST
Inp	904.00		NIST
Inp	909.00		NIST
Inp	915.00		NIST
Inp	903.00		NIST
Inp	889.00		NIST
Inp	896.00		NIST
Inp	902.00		NIST
Inp	889.00		NIST
Inp	880.00		NIST
Inp	889.00		NIST
Inp	900.00		NIST
Inp	900.00		NIST
Inp	888.00		NIST
Inp	906.00		NIST
Inp	897.00		NIST
Inp	886.00		NIST
Inp	900.00		NIST
Inp	879.00		NIST
Inp	894.00		NIST
Inp	882.00		NIST
Inp	906.00		NIST
Inp	Outlier 142.33		NIST
Inp	882.30		NIST
Inp	889.00		NIST
I	[1280.00; 1344.00]
I	1294.00		NIST
I	1307.00		NIST
I	1319.00		NIST
I	1319.00		NIST
I	1325.00		NIST
I	Outlier 1285.00		NIST
I	1327.00		NIST
I	1335.00		NIST
I	1318.00		NIST
I	1298.00		NIST
I	1301.00		NIST
I	1321.00		NIST
I	1322.00		NIST
I	1321.00		NIST
I	1296.00		NIST
I	1327.00		NIST
I	1303.00		NIST
I	1318.00		NIST
I	1308.00		NIST
I	1318.00		NIST
I	1321.00		NIST
I	1324.00		NIST
I	1325.00		NIST
I	1323.00		NIST
I	1290.00		NIST
I	1334.00		NIST
I	1332.00		NIST
I	1326.00		NIST
I	1331.00		NIST
I	1344.00		NIST
I	1310.00		NIST
I	1333.00		NIST
I	1335.00		NIST
I	1312.00		NIST
I	1334.00		NIST
I	1324.00		NIST
I	1328.00		NIST
I	1315.00		NIST
I	1313.00		NIST
I	1312.00		NIST
I	1316.00		NIST
I	1316.00		NIST
I	Outlier 1286.00		NIST
I	1328.00		NIST
I	1318.00		NIST
I	1319.00		NIST
I	1320.00		NIST
I	1320.00		NIST
I	1310.00		NIST
I	1326.00		NIST
I	1344.00		NIST
I	1322.00		NIST
I	1334.00		NIST
I	1326.00		NIST
I	1321.00		NIST
I	1332.00		NIST
I	1332.00		NIST
I	1332.00		NIST
I	Outlier 1280.00		NIST
I	1304.00		NIST
I	1318.00		NIST
I	1311.00		NIST
I	Outlier 1284.00		NIST
I	1322.00		NIST
I	1315.00		NIST
I	1290.00		NIST
I	1290.00		NIST
I	1318.00		NIST
I	1318.00		NIST
I	1326.00		NIST
I	1334.00		NIST
I	1334.00		NIST
I	1334.00		NIST
I	1334.00		NIST
I	1336.00		NIST
I	1318.00		NIST
I	1300.00		NIST
I	1312.00		NIST
I	1335.00		NIST
I	1326.00		NIST
I	1334.00		NIST
I	1304.00		NIST
I	1322.00		NIST
I	1324.00		NIST
I	1320.00		NIST
I	Outlier 1284.00		NIST
I	1293.00		NIST
I	1318.00		NIST
I	1320.00		NIST
I	Outlier 1286.00		NIST
I	1318.00		NIST
I	1318.00		NIST
I	1325.00		NIST
I	1298.00		NIST
I	1296.00		NIST
I	1318.00		NIST
I	1290.00		NIST
Tboil	[429.40; 434.20]	K
Tboil	432.00	K	KDB
Tboil	434.20	K	NIST
Tboil	431.15 ± 3.00	K	NIST
Tboil	432.65 ± 2.00	K	NIST
Tboil	433.55 ± 0.50	K	NIST
Tboil	432.85 ± 0.50	K	NIST
Tboil	432.55 ± 1.00	K	NIST
Tboil	434.15 ± 1.00	K	NIST
Tboil	429.65 ± 3.00	K	NIST
Tboil	431.85 ± 0.50	K	NIST
Tboil	429.40 ± 3.00	K	NIST
Tboil	432.15 ± 2.00	K	NIST
Tboil	430.65 ± 3.00	K	NIST
Tboil	434.15 ± 3.00	K	NIST
Tc	[608.30; 611.40]	K
Tc	608.30	K	KDB
Tc	608.30 ± 0.60	K	NIST
Tc	608.60 ± 0.60	K	NIST
Tc	608.30 ± 0.60	K	NIST
Tc	608.38	K	NIST
Tc	Outlier 611.40 ± 0.25	K	NIST
Tfus	243.00	K	KDB
Vc	[0.442; 0.442]	m3/kmol
Vc	0.442	m3/kmol	KDB
Vc	0.442	m3/kmol	NIST
Zc	0.2640090		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[248.00; 307.32]	J/mol×K	[451.50; 615.33]
Cp,gas	248.00	J/mol×K	451.50	Joback Calculated Property
Cp,gas	258.87	J/mol×K	478.81	Joback Calculated Property
Cp,gas	269.34	J/mol×K	506.11	Joback Calculated Property
Cp,gas	279.40	J/mol×K	533.42	Joback Calculated Property
Cp,gas	289.08	J/mol×K	560.72	Joback Calculated Property
Cp,gas	298.38	J/mol×K	588.03	Joback Calculated Property
Cp,gas	307.32	J/mol×K	615.33	Joback Calculated Property
η	[0.0028520; 0.0050230]	Pa×s	[298.15; 313.15]
η	0.0050030	Pa×s	298.15	Densities and viscosities of binary mixtures of ethylmethylketone and 2-alkanols; application of the ERAS model and cubic EOS
η	0.0050230	Pa×s	298.15	Densities and Viscosities of Binary Mixtures of Cyclohexanone and 2-Alkanols
η	0.0041520	Pa×s	303.15	Densities and viscosities of binary mixtures of ethylmethylketone and 2-alkanols; application of the ERAS model and cubic EOS
η	0.0041510	Pa×s	303.15	Densities and Viscosities of Binary Mixtures of Cyclohexanone and 2-Alkanols
η	0.0034780	Pa×s	308.15	Densities and viscosities of binary mixtures of ethylmethylketone and 2-alkanols; application of the ERAS model and cubic EOS
η	0.0034780	Pa×s	308.15	Densities and Viscosities of Binary Mixtures of Cyclohexanone and 2-Alkanols
η	0.0028530	Pa×s	313.15	Densities and viscosities of binary mixtures of ethylmethylketone and 2-alkanols; application of the ERAS model and cubic EOS
η	0.0028520	Pa×s	313.15	Densities and Viscosities of Binary Mixtures of Cyclohexanone and 2-Alkanols
ΔvapH	[51.60; 66.10]	kJ/mol	[291.00; 394.00]
ΔvapH	66.10	kJ/mol	291.00	NIST
ΔvapH	59.80	kJ/mol	378.00	NIST
ΔvapH	54.40	kJ/mol	392.00	NIST
ΔvapH	51.60	kJ/mol	394.00	NIST
n0	[1.41430; 1.42060]		[293.15; 308.15]
n0	1.42060		293.15	Densities, viscosities, excess molar volumes, and refractive indices of acetonitrile and 2-alkanols binary mixtures at different temperatures: Experimental results and application of the Prigogine Flory Patterson theory
n0	1.41880		298.15	Densities, viscosities, excess molar volumes, and refractive indices of acetonitrile and 2-alkanols binary mixtures at different temperatures: Experimental results and application of the Prigogine Flory Patterson theory
n0	1.41880		298.15	Densities, Viscosities, and Refractive Indices of Binary Mixtures of Acetophenone and 2-Alkanols
n0	1.41650		303.15	Densities, viscosities, excess molar volumes, and refractive indices of acetonitrile and 2-alkanols binary mixtures at different temperatures: Experimental results and application of the Prigogine Flory Patterson theory
n0	1.41430		308.15	Densities, viscosities, excess molar volumes, and refractive indices of acetonitrile and 2-alkanols binary mixtures at different temperatures: Experimental results and application of the Prigogine Flory Patterson theory
ρl	[789.38; 813.74]	kg/m3	[298.15; 328.15]
ρl	813.20	kg/m3	298.15	Thermodynamic Properties of Binary Mixtures Containing N,N-Dimethylacetamide + 2-Alkanol: Experimental Data and Modeling
ρl	813.74	kg/m3	298.15	Study of thermodynamic and transport properties of binary liquid mixtures of n-decane with hexan-2-ol, heptan-2-ol and octan-2-ol at T = 298.15 K. Experimental results and application of the Prigogine-Flory-Patterson theory
ρl	813.38	kg/m3	298.15	Densities and viscosities of the mixtures (formamide + 2-alkanol): Experimental and theoretical approaches
ρl	813.74	kg/m3	298.15	Densities, viscosities and ultrasonic velocities of binary mixtures of methylbenzene with hexan-2-ol, heptan-2-ol and octan-2-ol at T = 298.15 and 308.15K
ρl	813.36	kg/m3	298.15	The study of physico-chemical properties of binary systems consisting of N-Methylcyclohexylamine with 2-alkanols at T = (298.15-328.15) K
ρl	809.50	kg/m3	303.15	Densities and viscosities of the mixtures (formamide + 2-alkanol): Experimental and theoretical approaches
ρl	809.50	kg/m3	303.15	Thermodynamic Properties of Binary Mixtures Containing N,N-Dimethylacetamide + 2-Alkanol: Experimental Data and Modeling
ρl	804.88	kg/m3	308.15	Densities, viscosities and ultrasonic velocities of binary mixtures of methylbenzene with hexan-2-ol, heptan-2-ol and octan-2-ol at T = 298.15 and 308.15K
ρl	805.72	kg/m3	308.15	Densities and viscosities of the mixtures (formamide + 2-alkanol): Experimental and theoretical approaches
ρl	805.72	kg/m3	308.15	The study of physico-chemical properties of binary systems consisting of N-Methylcyclohexylamine with 2-alkanols at T = (298.15-328.15) K
ρl	805.70	kg/m3	308.15	Thermodynamic Properties of Binary Mixtures Containing N,N-Dimethylacetamide + 2-Alkanol: Experimental Data and Modeling
ρl	801.46	kg/m3	313.15	Densities and viscosities of the mixtures (formamide + 2-alkanol): Experimental and theoretical approaches
ρl	801.50	kg/m3	313.15	Thermodynamic Properties of Binary Mixtures Containing N,N-Dimethylacetamide + 2-Alkanol: Experimental Data and Modeling
ρl	797.65	kg/m3	318.15	The study of physico-chemical properties of binary systems consisting of N-Methylcyclohexylamine with 2-alkanols at T = (298.15-328.15) K
ρl	789.38	kg/m3	328.15	The study of physico-chemical properties of binary systems consisting of N-Methylcyclohexylamine with 2-alkanols at T = (298.15-328.15) K

Datasets

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
313.16	1003.00	802.5
313.16	2005.00	803.3
313.16	3002.00	804.0
313.16	4013.00	804.8
313.16	5001.00	805.5
313.16	5991.00	806.2
313.16	6993.00	806.9
313.16	7994.00	807.7
313.16	9011.00	808.4
313.16	9995.00	809.1
313.16	10990.00	809.8
313.16	11988.00	810.5
313.16	13003.00	811.2
313.16	13988.00	811.9
313.16	14992.00	812.6
313.16	15990.00	813.2
313.16	17012.00	813.9
313.16	17987.00	814.5
313.16	18982.00	815.2
313.16	20004.00	815.9
313.16	20996.00	816.5
313.16	21989.00	817.2
323.09	1026.00	794.4
323.09	2006.00	795.2
323.09	3018.00	796.0
323.09	4017.00	796.8
323.09	5005.00	797.5
323.09	6018.00	798.3
323.09	7002.00	799.1
323.09	8003.00	799.8
323.09	9017.00	800.6
323.09	10017.00	801.3
323.09	10994.00	802.0
323.09	11998.00	802.8
323.09	13028.00	803.5
323.09	13997.00	804.2
323.09	15005.00	804.9
323.09	16003.00	805.6
323.09	17013.00	806.3
323.09	18009.00	807.0
323.09	19003.00	807.6
323.09	20006.00	808.3
323.09	20998.00	808.9
323.09	22011.00	809.6
333.05	1047.00	786.1
333.05	2009.00	787.0
333.05	3005.00	787.8
333.05	4010.00	788.7
333.05	5015.00	789.5
333.05	6018.00	790.3
333.05	7022.00	791.1
333.05	8012.00	791.9
333.05	9031.00	792.8
333.05	10017.00	793.5
333.05	11080.00	794.3
333.05	12039.00	795.1
333.05	13026.00	795.8
333.05	14017.00	796.6
333.05	15024.00	797.3
333.05	16018.00	798.1
333.05	17020.00	798.8
333.05	18019.00	799.5
333.05	19029.00	800.2
333.05	20016.00	800.9
333.05	21037.00	801.7
333.05	22015.00	802.4
342.96	971.00	777.4
342.96	2038.00	778.5
342.96	3013.00	779.3
342.96	4034.00	780.2
342.96	5024.00	781.1
342.96	6033.00	782.0
342.96	7015.00	782.9
342.96	8023.00	783.8
342.96	9025.00	784.7
342.96	10020.00	785.4
342.96	11029.00	786.3
342.96	12020.00	787.1
342.96	13030.00	787.9
342.96	14039.00	788.7
342.96	15023.00	789.5
342.96	16026.00	790.3
342.96	17026.00	791.1
342.96	18034.00	791.9
342.96	19026.00	792.7
342.96	20040.00	793.5
342.96	21031.00	794.2
342.96	22028.00	795.0
352.85	1038.00	769.0
352.85	2045.00	770.0
352.85	3019.00	770.9
352.85	4058.00	771.9
352.85	5028.00	772.8
352.85	6028.00	773.7
352.85	7037.00	774.7
352.85	8022.00	775.5
352.85	9078.00	776.5
352.85	10037.00	777.3
352.85	11042.00	778.2
352.85	12042.00	779.0
352.85	13042.00	779.9
352.85	14040.00	780.8
352.85	15042.00	781.6
352.85	16053.00	782.5
352.85	17058.00	783.3
352.85	18042.00	784.1
352.85	19040.00	784.9
352.85	20070.00	785.7
352.85	21055.00	786.5
352.85	22050.00	787.3
362.72	1043.00	760.1
362.72	2049.00	761.2
362.72	3066.00	762.2
362.72	4062.00	763.2
362.72	5041.00	764.2
362.72	6045.00	765.2
362.72	7046.00	766.2
362.72	8042.00	767.2
362.72	9058.00	768.1
362.72	10038.00	769.0
362.72	11054.00	770.0
362.72	12046.00	770.9
362.72	13054.00	771.8
362.72	14048.00	772.7
362.72	15049.00	773.6
362.72	16050.00	774.5
362.72	17070.00	775.4
362.72	18065.00	776.2
362.72	19060.00	777.1
362.72	20081.00	777.9
362.72	21068.00	778.8
362.72	22063.00	779.6
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.65]	kPa	[335.65; 456.45]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.38938e+01
Coefficient B			-2.80782e+03
Coefficient C			-1.29285e+02
Temperature range, min.			335.65
Temperature range, max.			456.45
Pvap	1.33	kPa	335.65	Calculated Property
Pvap	3.06	kPa	349.07	Calculated Property
Pvap	6.38	kPa	362.49	Calculated Property
Pvap	12.29	kPa	375.92	Calculated Property
Pvap	22.12	kPa	389.34	Calculated Property
Pvap	37.59	kPa	402.76	Calculated Property
Pvap	60.76	kPa	416.18	Calculated Property
Pvap	94.10	kPa	429.61	Calculated Property
Pvap	140.38	kPa	443.03	Calculated Property
Pvap	202.65	kPa	456.45	Calculated Property
Pvap	[8.06e-04; 2994.69]	kPa	[243.00; 588.00]	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			1.14758e+02
Coefficient B			-1.04894e+04
Coefficient C			-1.44255e+01
Coefficient D			8.88948e-06
Coefficient E			0.00000e+00
Temperature range, min.			243.00
Temperature range, max.			588.00
Pvap	8.06e-04	kPa	243.00	Calculated Property
Pvap	0.04	kPa	281.33	Calculated Property
Pvap	0.71	kPa	319.67	Calculated Property
Pvap	5.86	kPa	358.00	Calculated Property
Pvap	29.69	kPa	396.33	Calculated Property
Pvap	107.38	kPa	434.67	Calculated Property
Pvap	305.58	kPa	473.00	Calculated Property
Pvap	732.16	kPa	511.33	Calculated Property
Pvap	1548.95	kPa	549.67	Calculated Property
Pvap	2994.69	kPa	588.00	Calculated Property

Similar Compounds

Find more compounds similar to 2-Heptanol.

Mixtures

• 2-Heptanol + Cyclohexanamine, N-methyl-
• 2-Heptanol + Cyclohexane, methyl-
• Acetonitrile + 2-Heptanol
• 2-Heptanol + Decane
• Toluene + 2-Heptanol
• Nitrogen + 2-Heptanol
• 2-Butanone + 2-Heptanol
• 2-Heptanol + Formamide
• 2-Heptanol + N,N-Dimethylacetamide
• 2-Heptanol + Acetophenone
• 2-Heptanol + Cyclohexanone
• 2-Heptanol + Ethanol, 2,2'-oxybis-

Sources

• KDB Vapor Pressure Data
• Cheméo Relay (1.0)
• Crippen Method
• Vapor liquid equilibria for nitrogen with 2-hexanol, 2-heptanol, or 2-octanol binary systems
• Densities, viscosities and ultrasonic velocities of binary mixtures of methylbenzene with hexan-2-ol, heptan-2-ol and octan-2-ol at T = 298.15 and 308.15K
• A thermodynamic study of the ketoreductase-catalyzed reduction of 2-alkanones in non-aqueous solvents
• Speeds of sound, isentropic compressibilities, viscosities and excess molar volumes of binary mixtures of methylcyclohexane + 2-alkanols or ethanol at T = 298.15 K
• Vapour pressures and heat capacity measurements on the C7 C9 secondary aliphatic alcohols
• Densities and derived thermodynamic properties of 1-heptanol and 2-heptanol at temperatures from 313 K to 363 K and pressures up to 22 MPa
• Study of thermodynamic and transport properties of binary liquid mixtures of n-decane with hexan-2-ol, heptan-2-ol and octan-2-ol at T = 298.15 K. Experimental results and application of the Prigogine-Flory-Patterson theory
• Densities and viscosities of the mixtures (formamide + 2-alkanol): Experimental and theoretical approaches
• The study of physico-chemical properties of binary systems consisting of N-Methylcyclohexylamine with 2-alkanols at T = (298.15-328.15) K
• Densities, viscosities, excess molar volumes, and refractive indices of acetonitrile and 2-alkanols binary mixtures at different temperatures: Experimental results and application of the Prigogine Flory Patterson theory
• Densities and viscosities of binary mixtures of ethylmethylketone and 2-alkanols; application of the ERAS model and cubic EOS
• Densities and Viscosities of Binary Mixtures of Cyclohexanone and 2-Alkanols
• Densities and Viscosities of Binary Mixtures Containing Diethylene Glycol and 2-Alkanol
• Thermodynamic Properties of Binary Mixtures Containing N,N-Dimethylacetamide + 2-Alkanol: Experimental Data and Modeling
• Densities, Viscosities, and Refractive Indices of Binary Mixtures of Acetophenone and 2-Alkanols
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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