Chemical Properties of 2-Pentanol (CAS 6032-29-7)

InChI

InChI=1S/C5H12O/c1-3-4-5(2)6/h5-6H,3-4H2,1-2H3

InChI Key

JYVLIDXNZAXMDK-UHFFFAOYSA-N

Formula

C5H12O

SMILES

CCCC(C)O

Molecular Weight¹

88.15

CAS

6032-29-7

Other Names

• (R,S)-2-pentanol
• 1-Methyl-1-butanol
• 1-Methylbutanol
• 2-Pentyl alcohol
• Isoamyl alcohol, secondary
• Methylpropylcarbinol
• Pentanol-2
• dl-2-pentanol
• n-C3H7CH(OH)CH3
• pentan-2-ol
• sec-Amyl alcohol
• sec-Pentanol
• sec-Pentyl alcohol
• sec-n-Amyl alcohol

• ω : Acentric Factor.
• α_p : Isobaric thermal expansion coefficient (1/K).
• 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_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).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• 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.
• S°_gas : 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).
• 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	0.5494		Relay (1.0) Calculated Property
ΔcH°liquid	-3315.40 ± 0.67	kJ/mol	NIST
Cp,liquid	235.30	J/mol×K	Partial Molar Heat Capacities and Partial Molar Volumes of All of the Isomeric (C3 to C5) Alkanols at Infinite Dilution in Water at 298.15 K
η	0.0034210	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°	-148.04	kJ/mol	Joback Calculated Property
ΔfH°gas	[-314.60; -312.70]	kJ/mol
ΔfH°gas	-312.70	kJ/mol	NIST
ΔfH°gas	-313.80 ± 1.10	kJ/mol	NIST
ΔfH°gas	-314.60 ± 1.50	kJ/mol	NIST
ΔfH°liquid	[-367.10; -365.20]	kJ/mol
ΔfH°liquid	-365.20 ± 1.10	kJ/mol	NIST
ΔfH°liquid	-366.40 ± 1.70	kJ/mol	NIST
ΔfH°liquid	-367.10 ± 0.75	kJ/mol	NIST
ΔfusH°	9.27	kJ/mol	Joback Calculated Property
ΔvapH°	[52.60; 54.20]	kJ/mol
ΔvapH°	53.60	kJ/mol	NIST
ΔvapH°	54.20 ± 0.20	kJ/mol	NIST
ΔvapH°	52.60 ± 1.30	kJ/mol	NIST
ΔvapH°	52.60 ± 1.30	kJ/mol	NIST
ΔvapH°	53.00	kJ/mol	NIST
IE	[9.78; 10.27]	eV
IE	9.78 ± 0.03	eV	NIST
IE	9.78 ± 0.07	eV	NIST
IE	9.78	eV	NIST
IE	10.27	eV	NIST
log10WS	[-0.29; -0.29]
log10WS	-0.29		Aq. Solubility Prediction
log10WS	-0.29		Estimated Solubility
logPoct/wat	1.167		Crippen Calculated Property
McVol	87.180	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
NFPA Health	1		KDB
Pc	[3640.00; 3710.00]	kPa
Pc	3675.00	kPa	KDB
Pc	3680.00 ± 20.00	kPa	NIST
Pc	3640.00 ± 40.00	kPa	NIST
Pc	3710.00 ± 20.00	kPa	NIST
Pc	3710.00 ± 20.00	kPa	NIST
ρc	[267.97; 267.97]	kg/m3
ρc	267.97 ± 1.76	kg/m3	NIST
ρc	267.97 ± 20.27	kg/m3	NIST
Inp	[661.00; 730.00]
Inp	692.00		NIST
Inp	697.00		NIST
Inp	683.00		NIST
Inp	692.00		NIST
Inp	701.00		NIST
Inp	704.00		NIST
Inp	697.00		NIST
Inp	683.00		NIST
Inp	692.00		NIST
Inp	701.00		NIST
Inp	704.00		NIST
Inp	697.00		NIST
Inp	683.00		NIST
Inp	685.00		NIST
Inp	666.00		NIST
Inp	671.00		NIST
Inp	689.00		NIST
Inp	685.00		NIST
Inp	685.00		NIST
Inp	665.00		NIST
Inp	682.00		NIST
Inp	Outlier 661.00		NIST
Inp	687.00		NIST
Inp	688.00		NIST
Inp	705.00		NIST
Inp	685.00		NIST
Inp	688.00		NIST
Inp	706.00		NIST
Inp	702.00		NIST
Inp	Outlier 730.00		NIST
Inp	705.00		NIST
Inp	664.00		NIST
Inp	662.00		NIST
Inp	687.00		NIST
Inp	664.00		NIST
Inp	717.00		NIST
Inp	717.00		NIST
Inp	691.00		NIST
Inp	685.00		NIST
Inp	682.00		NIST
Inp	682.00		NIST
Inp	718.00		NIST
Inp	Outlier 730.00		NIST
Inp	712.00		NIST
Inp	689.00		NIST
Inp	703.00		NIST
Inp	704.00		NIST
Inp	700.00		NIST
Inp	703.00		NIST
Inp	706.00		NIST
Inp	718.00		NIST
Inp	672.00		NIST
Inp	674.00		NIST
Inp	674.00		NIST
Inp	674.00		NIST
Inp	685.00		NIST
Inp	677.00		NIST
Inp	695.00		NIST
Inp	699.00		NIST
Inp	699.00		NIST
Inp	689.00		NIST
Inp	701.00		NIST
Inp	706.00		NIST
Inp	700.00		NIST
Inp	689.00		NIST
Inp	689.00		NIST
Inp	689.00		NIST
Inp	689.00		NIST
Inp	685.00		NIST
Inp	700.00		NIST
Inp	683.00		NIST
Inp	706.00		NIST
Inp	671.00		NIST
Inp	683.00		NIST
Inp	695.00		NIST
Inp	710.00		NIST
Inp	677.00		NIST
Inp	685.00		NIST
Inp	689.00		NIST
Inp	706.00		NIST
Inp	662.00		NIST
Inp	691.00		NIST
Inp	703.00		NIST
Inp	718.00		NIST
Inp	685.00		NIST
I	[1081.00; 1153.00]
I	1130.00		NIST
I	1129.00		NIST
I	1121.00		NIST
I	1130.00		NIST
I	1129.00		NIST
I	1121.00		NIST
I	1112.00		NIST
I	1115.00		NIST
I	1117.00		NIST
I	1117.00		NIST
I	1112.00		NIST
I	1113.00		NIST
I	1100.00		NIST
I	1130.00		NIST
I	1138.00		NIST
I	1119.00		NIST
I	1138.00		NIST
I	1100.00		NIST
I	1096.00		NIST
I	1094.00		NIST
I	1120.00		NIST
I	1122.00		NIST
I	1120.00		NIST
I	1105.00		NIST
I	1127.00		NIST
I	1107.00		NIST
I	1116.00		NIST
I	1107.00		NIST
I	1107.00		NIST
I	1109.00		NIST
I	1110.00		NIST
I	1109.00		NIST
I	1109.00		NIST
I	1116.00		NIST
I	1139.00		NIST
I	1142.00		NIST
I	1139.00		NIST
I	1122.00		NIST
I	1109.00		NIST
I	1109.00		NIST
I	1118.00		NIST
I	Outlier 1153.00		NIST
I	1112.00		NIST
I	1135.00		NIST
I	1136.00		NIST
I	1124.00		NIST
I	Outlier 1081.00		NIST
I	1112.00		NIST
I	1123.00		NIST
I	1123.00		NIST
I	1125.00		NIST
I	1114.00		NIST
I	1118.00		NIST
I	1130.00		NIST
I	1142.00		NIST
I	1117.00		NIST
I	1122.00		NIST
I	1138.00		NIST
I	1121.00		NIST
I	1116.00		NIST
I	1135.00		NIST
I	1136.00		NIST
I	1113.00		NIST
I	1130.00		NIST
I	1094.00		NIST
I	1117.00		NIST
I	1130.00		NIST
I	1119.00		NIST
I	1135.00		NIST
I	1120.00		NIST
I	Outlier 1091.00		NIST
I	1116.00		NIST
I	1100.00		NIST
I	1116.00		NIST
I	Outlier 1085.00		NIST
I	1122.00		NIST
I	1126.00		NIST
I	1129.00		NIST
I	1142.00		NIST
I	1140.00		NIST
I	1124.00		NIST
I	Outlier 1148.00		NIST
I	1121.00		NIST
I	Outlier 1091.00		NIST
I	1105.00		NIST
I	1107.00		NIST
I	1110.00		NIST
I	1116.00		NIST
I	1135.00		NIST
I	1123.00		NIST
I	1130.00		NIST
I	1121.00		NIST
I	1116.00		NIST
I	1122.00		NIST
I	1124.00		NIST
I	1107.00		NIST
S°gas	392.00 ± 0.90	J/mol×K	NIST
Tboil	[364.15; 400.65]	K
Tboil	392.40	K	KDB
Tboil	392.10	K	NIST
Tboil	391.40 ± 1.00	K	NIST
Tboil	391.15 ± 2.00	K	NIST
Tboil	388.20 ± 3.00	K	NIST
Tboil	391.15 ± 4.00	K	NIST
Tboil	392.45 ± 1.00	K	NIST
Tboil	392.45 ± 0.30	K	NIST
Tboil	392.15 ± 1.00	K	NIST
Tboil	392.35 ± 0.50	K	NIST
Tboil	391.65 ± 1.00	K	NIST
Tboil	392.65 ± 0.50	K	NIST
Tboil	390.40 ± 2.00	K	NIST
Tboil	392.35 ± 0.50	K	NIST
Tboil	392.95 ± 0.50	K	NIST
Tboil	Outlier 364.15 ± 2.00	K	NIST
Tboil	392.50 ± 1.00	K	NIST
Tboil	392.00 ± 0.50	K	NIST
Tboil	392.65 ± 1.00	K	NIST
Tboil	392.60 ± 0.50	K	NIST
Tboil	392.15 ± 1.00	K	NIST
Tboil	392.70 ± 0.30	K	NIST
Tboil	393.00 ± 0.10	K	NIST
Tboil	392.15 ± 1.00	K	NIST
Tboil	392.45 ± 0.40	K	NIST
Tboil	392.15 ± 2.00	K	NIST
Tboil	392.15 ± 2.00	K	NIST
Tboil	392.45 ± 0.50	K	NIST
Tboil	392.00 ± 1.50	K	NIST
Tboil	391.00 ± 1.00	K	NIST
Tboil	Outlier 400.65 ± 3.00	K	NIST
Tboil	392.15 ± 1.00	K	NIST
Tboil	392.36 ± 0.20	K	NIST
Tboil	392.15 ± 2.00	K	NIST
Tboil	392.15 ± 1.00	K	NIST
Tboil	392.15 ± 1.00	K	NIST
Tboil	392.35 ± 0.50	K	NIST
Tboil	392.15 ± 1.00	K	NIST
Tboil	392.05 ± 0.50	K	NIST
Tboil	393.65 ± 2.00	K	NIST
Tboil	393.15 ± 2.00	K	NIST
Tboil	392.15 ± 1.00	K	NIST
Tboil	391.15 ± 1.00	K	NIST
Tboil	392.15 ± 2.00	K	NIST
Tc	[560.00; 560.40]	K
Tc	560.30	K	KDB
Tc	560.30 ± 0.50	K	NIST
Tc	Outlier 560.00 ± 0.70	K	NIST
Tc	560.40 ± 0.60	K	NIST
Tc	560.40 ± 0.60	K	NIST
Tc	560.40	K	NIST
Tc	560.40 ± 0.25	K	NIST
Tfus	[200.00; 211.65]	K
Tfus	200.00	K	KDB
Tfus	211.65	K	Aq. Solubility Prediction
Vc	[0.329; 0.329]	m3/kmol
Vc	0.329	m3/kmol	KDB
Vc	0.329	m3/kmol	NIST
Zc	0.2595350		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[138.34; 235.81]	J/mol×K	[134.18; 301.07]
Cp,liquid	138.36	J/mol×K	134.18	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	145.14	J/mol×K	134.47	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	146.40	J/mol×K	135.24	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	146.52	J/mol×K	136.00	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	138.34	J/mol×K	136.05	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	145.03	J/mol×K	136.39	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	146.29	J/mol×K	137.22	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	138.35	J/mol×K	137.97	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	145.17	J/mol×K	138.36	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	146.59	J/mol×K	138.84	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	146.22	J/mol×K	139.21	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	138.69	J/mol×K	139.90	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	145.48	J/mol×K	140.33	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	146.34	J/mol×K	141.20	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	146.74	J/mol×K	141.77	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	139.02	J/mol×K	141.83	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	145.81	J/mol×K	142.30	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	146.48	J/mol×K	143.19	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	139.32	J/mol×K	143.77	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	146.91	J/mol×K	144.73	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	146.45	J/mol×K	145.18	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	146.59	J/mol×K	147.18	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	147.17	J/mol×K	147.68	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	146.66	J/mol×K	149.17	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	147.42	J/mol×K	150.63	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	146.74	J/mol×K	151.16	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	146.86	J/mol×K	153.16	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	147.65	J/mol×K	153.58	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	147.04	J/mol×K	155.16	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	148.06	J/mol×K	156.54	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	147.26	J/mol×K	157.16	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	147.41	J/mol×K	159.16	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	148.35	J/mol×K	159.50	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	147.59	J/mol×K	161.15	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	148.75	J/mol×K	162.46	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	147.87	J/mol×K	163.15	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	148.07	J/mol×K	165.15	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	149.14	J/mol×K	165.42	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	148.38	J/mol×K	167.15	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	149.64	J/mol×K	168.38	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	148.62	J/mol×K	169.15	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	148.98	J/mol×K	171.15	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	150.12	J/mol×K	171.34	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	149.17	J/mol×K	173.15	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	150.62	J/mol×K	174.31	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	149.61	J/mol×K	175.15	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	150.03	J/mol×K	177.14	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	151.24	J/mol×K	177.27	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	150.37	J/mol×K	179.14	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	151.84	J/mol×K	180.22	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	150.83	J/mol×K	181.14	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	151.22	J/mol×K	183.13	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	152.41	J/mol×K	183.15	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	151.66	J/mol×K	185.13	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	153.18	J/mol×K	186.06	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	152.22	J/mol×K	187.13	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	153.85	J/mol×K	188.97	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	152.69	J/mol×K	189.12	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	153.28	J/mol×K	191.11	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	154.61	J/mol×K	191.86	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	153.79	J/mol×K	193.10	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	155.46	J/mol×K	194.73	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	154.43	J/mol×K	195.09	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	155.04	J/mol×K	197.08	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	156.28	J/mol×K	197.60	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	155.64	J/mol×K	199.07	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	157.17	J/mol×K	200.45	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	156.37	J/mol×K	201.05	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	157.14	J/mol×K	203.04	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	158.12	J/mol×K	203.28	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	157.90	J/mol×K	205.02	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	159.16	J/mol×K	206.11	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	158.71	J/mol×K	207.00	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	160.23	J/mol×K	208.92	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	159.59	J/mol×K	208.98	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	160.43	J/mol×K	210.96	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	161.38	J/mol×K	211.71	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	161.43	J/mol×K	212.93	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	162.60	J/mol×K	214.50	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	162.36	J/mol×K	214.90	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	163.53	J/mol×K	216.87	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	163.98	J/mol×K	217.27	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	164.58	J/mol×K	218.83	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	165.38	J/mol×K	220.03	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	165.86	J/mol×K	220.79	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	167.19	J/mol×K	222.74	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	166.74	J/mol×K	222.77	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	168.30	J/mol×K	224.69	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	168.21	J/mol×K	225.50	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	169.58	J/mol×K	226.64	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	169.75	J/mol×K	228.21	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	170.97	J/mol×K	228.58	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	172.40	J/mol×K	230.52	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	171.38	J/mol×K	230.92	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	173.26	J/mol×K	232.46	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	173.02	J/mol×K	233.61	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	174.28	J/mol×K	234.41	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	174.82	J/mol×K	236.28	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	175.25	J/mol×K	236.37	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	176.25	J/mol×K	238.35	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	176.57	J/mol×K	238.94	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	177.32	J/mol×K	240.33	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	178.24	J/mol×K	241.59	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	178.65	J/mol×K	242.31	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	179.98	J/mol×K	244.22	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	180.19	J/mol×K	244.29	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	181.71	J/mol×K	246.27	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	181.91	J/mol×K	246.84	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	183.24	J/mol×K	248.24	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	183.85	J/mol×K	249.45	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	184.81	J/mol×K	250.22	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	185.96	J/mol×K	252.04	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	186.49	J/mol×K	252.19	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	187.53	J/mol×K	254.17	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	187.26	J/mol×K	254.62	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	189.21	J/mol×K	256.15	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	189.40	J/mol×K	257.20	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	190.90	J/mol×K	258.13	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	191.63	J/mol×K	259.75	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	192.75	J/mol×K	260.11	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	194.51	J/mol×K	262.08	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	193.87	J/mol×K	262.30	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	196.40	J/mol×K	264.06	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	196.18	J/mol×K	264.83	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	198.15	J/mol×K	266.04	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	198.56	J/mol×K	267.34	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	200.17	J/mol×K	268.01	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	201.01	J/mol×K	269.84	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	202.16	J/mol×K	269.99	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	204.25	J/mol×K	271.96	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	203.73	J/mol×K	272.33	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	206.27	J/mol×K	273.94	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	206.33	J/mol×K	274.80	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	208.32	J/mol×K	275.91	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	208.61	J/mol×K	277.26	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	210.50	J/mol×K	277.88	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	211.18	J/mol×K	279.70	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	212.62	J/mol×K	279.86	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	214.76	J/mol×K	281.83	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	213.77	J/mol×K	282.13	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	216.99	J/mol×K	283.81	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	216.55	J/mol×K	284.54	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	219.38	J/mol×K	285.79	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	219.25	J/mol×K	286.94	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	221.67	J/mol×K	287.77	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	222.07	J/mol×K	289.33	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	224.09	J/mol×K	289.75	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	224.87	J/mol×K	291.70	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	226.30	J/mol×K	291.73	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	228.63	J/mol×K	293.71	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	227.43	J/mol×K	294.06	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	231.18	J/mol×K	295.69	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	230.08	J/mol×K	296.41	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	233.65	J/mol×K	297.66	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	233.00	J/mol×K	298.75	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	235.81	J/mol×K	299.65	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Cp,liquid	235.62	J/mol×K	301.07	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
η	[0.0013900; 0.0040010]	Pa×s	[293.15; 323.15]
η	0.0040010	Pa×s	293.15	Viscosities, Densities, and Speed of Sound of the Cycloalkanes with Secondary Alcohols at T = (293.15, 298.15, and 303.15) K: New UNIFAC-VISCO Interaction Parameters
η	0.0040010	Pa×s	293.15	Viscosity, density, and speed of sound of methylcyclopentane with primary and secondary alcohols at T = (293.15, 298.15, and 303.15) K
η	0.0040010	Pa×s	293.15	Dynamic Viscosities of 2-Pentanol with Alkanes (Octane, Decane, and Dodecane) at Three Temperatures T ) (293.15, 298.15, and 303.15) K. New UNIFAC-VISCO Interaction Parameters
η	0.0034780	Pa×s	298.15	Densities and viscosities of binary mixtures of ethylmethylketone and 2-alkanols; application of the ERAS model and cubic EOS
η	0.0032730	Pa×s	298.15	Viscosity, density, and speed of sound of methylcyclopentane with primary and secondary alcohols at T = (293.15, 298.15, and 303.15) K
η	0.0034990	Pa×s	298.15	Densities and Viscosities of Binary Mixtures of Cyclohexanone and 2-Alkanols
η	0.0033200	Pa×s	298.15	Studies on physicochemical behavior of binary mixtures containing propanal and Alkan-2-ol
η	0.0032730	Pa×s	298.15	Viscosities, Densities, and Speed of Sound of the Cycloalkanes with Secondary Alcohols at T = (293.15, 298.15, and 303.15) K: New UNIFAC-VISCO Interaction Parameters
η	0.0032730	Pa×s	298.15	Dynamic Viscosities of 2-Pentanol with Alkanes (Octane, Decane, and Dodecane) at Three Temperatures T ) (293.15, 298.15, and 303.15) K. New UNIFAC-VISCO Interaction Parameters
η	0.0027080	Pa×s	303.15	Dynamic Viscosities of 2-Pentanol with Alkanes (Octane, Decane, and Dodecane) at Three Temperatures T ) (293.15, 298.15, and 303.15) K. New UNIFAC-VISCO Interaction Parameters
η	0.0028010	Pa×s	303.15	Densities and viscosities of binary mixtures of ethylmethylketone and 2-alkanols; application of the ERAS model and cubic EOS
η	0.0028010	Pa×s	303.15	Densities and Viscosities of Binary Mixtures of Cyclohexanone and 2-Alkanols
η	0.0027740	Pa×s	303.15	Viscosity, density, and speed of sound of methylcyclopentane with primary and secondary alcohols at T = (293.15, 298.15, and 303.15) K
η	0.0027740	Pa×s	303.15	Viscosities, Densities, and Speed of Sound of the Cycloalkanes with Secondary Alcohols at T = (293.15, 298.15, and 303.15) K: New UNIFAC-VISCO Interaction Parameters
η	0.0028100	Pa×s	303.15	Studies on physicochemical behavior of binary mixtures containing propanal and Alkan-2-ol
η	0.0023700	Pa×s	308.15	Studies on physicochemical behavior of binary mixtures containing propanal and Alkan-2-ol
η	0.0023350	Pa×s	308.15	Densities and viscosities of binary mixtures of ethylmethylketone and 2-alkanols; application of the ERAS model and cubic EOS
η	0.0023340	Pa×s	308.15	Densities and Viscosities of Binary Mixtures of Cyclohexanone and 2-Alkanols
η	0.0019900	Pa×s	313.15	Studies on physicochemical behavior of binary mixtures containing propanal and Alkan-2-ol
η	0.0019930	Pa×s	313.15	Densities and viscosities of binary mixtures of ethylmethylketone and 2-alkanols; application of the ERAS model and cubic EOS
η	0.0019930	Pa×s	313.15	Densities and Viscosities of Binary Mixtures of Cyclohexanone and 2-Alkanols
η	0.0016600	Pa×s	318.15	Studies on physicochemical behavior of binary mixtures containing propanal and Alkan-2-ol
η	0.0013900	Pa×s	323.15	Studies on physicochemical behavior of binary mixtures containing propanal and Alkan-2-ol
ΔfusH	[8.48; 8.48]	kJ/mol	[200.00; 200.00]
ΔfusH	8.48	kJ/mol	200.00	NIST
ΔfusH	8.48	kJ/mol	200.00	NIST
ΔvapH	[45.40; 58.90]	kJ/mol	[313.00; 368.00]
ΔvapH	52.70 ± 0.20	kJ/mol	313.00	NIST
ΔvapH	50.90 ± 0.20	kJ/mol	328.00	NIST
ΔvapH	58.90	kJ/mol	333.50	NIST
ΔvapH	53.70	kJ/mol	340.50	NIST
ΔvapH	49.00 ± 0.20	kJ/mol	343.00	NIST
ΔvapH	54.00	kJ/mol	345.50	NIST
ΔvapH	51.20	kJ/mol	357.50	NIST
ΔvapH	50.30	kJ/mol	357.50	NIST
ΔvapH	46.90 ± 0.10	kJ/mol	358.00	NIST
ΔvapH	45.40 ± 0.10	kJ/mol	368.00	NIST
Pvap	[2.13; 101.38]	kPa	[313.15; 392.26]
Pvap	2.29	kPa	313.15	Thermodynamic behaviour of second generation biofuels: Vapour liquid equilibria and excess enthalpies of the binary mixtures 2-pentanol and n-heptane or 2,2,4-trimethylpentane
Pvap	2.13	kPa	313.15	Vapor-Liquid Equilibria in Binary Systems Formed by n-Hexane with Alcohols
Pvap	2.29	kPa	313.15	Characterizing second generation biofuels: Excess enthalpies and vapour-liquid equilibria of the binary mixtures containing 1-pentanol or 2-pentanol and n-hexane
Pvap	4.16	kPa	323.15	Vapor-Liquid Equilibria in Binary Systems Formed by n-Hexane with Alcohols
Pvap	4.16	kPa	323.84	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	4.41	kPa	324.19	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	4.39	kPa	324.55	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	4.67	kPa	325.09	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	4.93	kPa	326.00	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	4.89	kPa	326.22	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	5.27	kPa	326.99	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	5.20	kPa	327.15	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	5.43	kPa	327.64	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	5.71	kPa	328.19	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	5.64	kPa	328.23	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	5.91	kPa	329.05	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	5.95	kPa	329.11	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	6.04	kPa	329.11	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	6.16	kPa	329.66	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	6.33	kPa	329.90	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	6.71	kPa	330.86	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	7.08	kPa	331.78	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	7.17	kPa	332.29	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	7.40	kPa	332.55	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	7.31	kPa	332.61	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	7.43	kPa	332.92	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	7.52	kPa	333.15	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	7.57	kPa	333.15	Vapor-Liquid Equilibria in Binary Systems Formed by n-Hexane with Alcohols
Pvap	7.76	kPa	333.37	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	7.99	kPa	333.88	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	8.33	kPa	334.61	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	8.77	kPa	335.52	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	9.17	kPa	336.34	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	9.19	kPa	336.37	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	9.59	kPa	337.20	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	9.95	kPa	337.85	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	9.99	kPa	338.15	Vapor-Liquid Equilibria in Binary Systems Formed by n-Hexane with Alcohols
Pvap	10.43	kPa	338.74	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	10.81	kPa	339.44	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	11.21	kPa	340.10	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	11.67	kPa	340.82	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	12.11	kPa	341.54	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	12.52	kPa	342.20	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	12.77	kPa	342.83	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	12.97	kPa	342.88	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	13.00	kPa	343.15	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	13.07	kPa	343.26	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	13.11	kPa	343.30	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	13.16	kPa	343.38	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	13.99	kPa	344.38	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	14.65	kPa	345.27	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	15.31	kPa	346.15	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	15.96	kPa	347.02	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	16.63	kPa	347.80	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	17.32	kPa	348.68	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	17.95	kPa	349.38	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	18.63	kPa	350.16	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	18.66	kPa	350.91	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	19.31	kPa	350.93	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	19.96	kPa	351.64	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	20.00	kPa	351.88	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	20.43	kPa	352.33	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	20.65	kPa	352.60	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	20.72	kPa	352.70	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	20.83	kPa	352.76	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	20.96	kPa	352.89	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	21.12	kPa	353.05	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	21.19	kPa	353.10	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	21.20	kPa	353.15	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	21.40	kPa	353.35	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	21.33	kPa	353.74	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	22.16	kPa	354.12	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	22.55	kPa	354.47	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	22.83	kPa	354.72	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	23.55	kPa	355.42	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	24.12	kPa	355.92	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	24.00	kPa	356.29	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	24.44	kPa	356.39	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	24.84	kPa	356.55	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	25.05	kPa	356.60	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	25.47	kPa	357.15	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	26.20	kPa	357.76	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	26.00	kPa	357.79	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	26.75	kPa	358.23	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	26.66	kPa	358.61	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	27.45	kPa	358.83	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	27.47	kPa	358.86	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	27.32	kPa	358.88	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	27.45	kPa	359.01	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	28.19	kPa	359.53	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	28.67	kPa	359.91	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	29.25	kPa	360.35	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	29.41	kPa	360.50	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	30.03	kPa	360.81	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	30.29	kPa	361.12	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	30.00	kPa	361.26	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	30.68	kPa	361.45	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	31.59	kPa	362.10	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	32.13	kPa	362.50	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	32.55	kPa	362.76	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	32.73	kPa	362.93	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	33.35	kPa	363.38	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	33.33	kPa	363.69	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	34.05	kPa	363.85	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	34.64	kPa	364.28	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	35.08	kPa	364.38	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	35.47	kPa	364.84	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	35.95	kPa	365.13	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	36.71	kPa	365.62	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	36.66	kPa	365.92	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	37.56	kPa	366.00	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	37.32	kPa	366.01	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	37.95	kPa	366.40	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	38.64	kPa	366.86	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	39.31	kPa	367.24	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	40.03	kPa	367.49	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	39.97	kPa	367.65	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	40.00	kPa	368.00	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	40.64	kPa	368.06	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	41.27	kPa	368.44	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	41.96	kPa	368.85	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	42.51	kPa	369.03	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	42.73	kPa	369.31	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	43.23	kPa	369.58	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	44.05	kPa	370.05	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	44.00	kPa	370.31	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	44.75	kPa	370.46	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	45.07	kPa	370.52	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	45.40	kPa	370.74	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	45.91	kPa	371.07	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	46.64	kPa	371.47	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	47.54	kPa	371.77	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	47.45	kPa	371.82	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	47.93	kPa	372.15	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	48.00	kPa	372.45	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	48.64	kPa	372.50	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	49.31	kPa	372.91	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	50.02	kPa	373.05	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	49.87	kPa	373.16	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	50.71	kPa	373.57	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	51.25	kPa	373.88	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	52.03	kPa	374.25	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	52.58	kPa	374.33	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	52.00	kPa	374.46	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	52.55	kPa	374.47	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	53.37	kPa	374.85	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	53.95	kPa	375.14	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	54.67	kPa	375.44	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	55.03	kPa	375.51	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	55.37	kPa	375.83	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	56.01	kPa	376.13	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	55.99	kPa	376.35	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	56.71	kPa	376.47	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	57.48	kPa	376.68	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	57.36	kPa	376.74	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	58.00	kPa	377.07	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	58.64	kPa	377.32	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	59.32	kPa	377.65	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	60.03	kPa	377.81	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	59.97	kPa	377.91	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	59.99	kPa	378.13	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	60.67	kPa	378.22	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	61.40	kPa	378.56	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	61.97	kPa	378.81	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	62.45	kPa	378.95	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	62.61	kPa	379.04	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	63.39	kPa	379.39	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	63.91	kPa	379.60	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	64.60	kPa	379.89	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	65.05	kPa	379.97	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	65.20	kPa	380.13	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	65.33	kPa	380.36	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	65.99	kPa	380.47	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	66.63	kPa	380.70	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	67.31	kPa	381.00	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	67.58	kPa	381.01	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	68.01	kPa	381.26	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	68.67	kPa	381.53	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	69.31	kPa	381.76	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	70.03	kPa	381.96	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	70.21	kPa	382.08	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	70.63	kPa	382.28	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	70.66	kPa	382.45	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	71.31	kPa	382.55	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	71.95	kPa	382.78	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	72.56	kPa	382.90	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	72.65	kPa	383.05	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	73.35	kPa	383.29	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	73.93	kPa	383.53	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	74.63	kPa	383.76	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	75.05	kPa	383.88	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	75.48	kPa	384.09	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	75.99	kPa	384.26	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	75.99	kPa	384.42	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	76.63	kPa	384.50	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	77.35	kPa	384.74	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	77.59	kPa	384.79	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	77.93	kPa	384.95	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	79.27	kPa	385.42	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	80.03	kPa	385.64	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	80.00	kPa	385.65	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	80.56	kPa	385.87	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	81.79	kPa	386.24	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	81.33	kPa	386.27	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	81.88	kPa	386.32	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	82.68	kPa	386.54	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	82.58	kPa	386.56	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	83.23	kPa	386.76	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	84.05	kPa	386.96	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	85.01	kPa	387.35	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	85.27	kPa	387.37	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	86.61	kPa	387.80	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	87.55	kPa	388.19	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	88.00	kPa	388.23	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	87.99	kPa	388.47	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	89.39	kPa	388.66	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	90.09	kPa	389.00	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	90.69	kPa	389.07	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	92.16	kPa	389.51	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	92.52	kPa	389.76	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	93.44	kPa	389.90	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	94.61	kPa	390.26	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	94.66	kPa	390.53	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	95.02	kPa	390.55	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	95.95	kPa	390.65	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	97.27	kPa	391.05	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	97.55	kPa	391.31	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	97.33	kPa	391.32	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	98.71	kPa	391.46	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	100.03	kPa	392.07	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	101.38	kPa	392.26	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
n0	[1.37030; 1.40600]		[293.15; 318.15]
n0	1.40600		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	1.40450		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	1.40450		298.15	Densities, Viscosities, and Refractive Indices of Binary Mixtures of Acetophenone and 2-Alkanols
n0	1.40320		298.15	Densities, Viscosities, and Refractive Indices of Binary Mixtures of Methyl Ethyl Ketone + Pentanol Isomers at Different Temperatures
n0	1.40490		298.20	Experimental and modeling study of liquid phase equilibria for (water + phosphoric acid + sec-alcohols) systems
n0	1.40216		303.15	Liquid-liquid equilibria for ternary mixtures of 1-alkyl-3-methyl imidazolium bis{(trifluoromethyl)sulfonyl}imides, n-hexane and organic compounds at 303.15 K and 0.1 MPa
n0	1.37240		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	1.37030		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
n0	1.39900		308.15	Densities, Viscosities, and Refractive Indices of Binary Mixtures of Methyl Ethyl Ketone + Pentanol Isomers at Different Temperatures
n0	1.39500		318.15	Densities, Viscosities, and Refractive Indices of Binary Mixtures of Methyl Ethyl Ketone + Pentanol Isomers at Different Temperatures
ρl	[770.37; 824.00]	kg/m3	[273.65; 338.15]
ρl	824.00	kg/m3	273.65	Temperature of maximum density for aqueous mixtures of three pentanol isomers
ρl	823.60	kg/m3	274.15	Temperature of maximum density for aqueous mixtures of three pentanol isomers
ρl	823.20	kg/m3	274.65	Temperature of maximum density for aqueous mixtures of three pentanol isomers
ρl	822.80	kg/m3	275.15	Temperature of maximum density for aqueous mixtures of three pentanol isomers
ρl	822.50	kg/m3	275.65	Temperature of maximum density for aqueous mixtures of three pentanol isomers
ρl	822.10	kg/m3	276.15	Temperature of maximum density for aqueous mixtures of three pentanol isomers
ρl	821.70	kg/m3	276.65	Temperature of maximum density for aqueous mixtures of three pentanol isomers
ρl	821.30	kg/m3	277.15	Temperature of maximum density for aqueous mixtures of three pentanol isomers
ρl	820.90	kg/m3	277.65	Temperature of maximum density for aqueous mixtures of three pentanol isomers
ρl	820.60	kg/m3	278.15	Temperature of maximum density for aqueous mixtures of three pentanol isomers
ρl	820.20	kg/m3	278.65	Temperature of maximum density for aqueous mixtures of three pentanol isomers
ρl	819.80	kg/m3	279.15	Temperature of maximum density for aqueous mixtures of three pentanol isomers
ρl	819.40	kg/m3	279.65	Temperature of maximum density for aqueous mixtures of three pentanol isomers
ρl	819.10	kg/m3	280.15	Temperature of maximum density for aqueous mixtures of three pentanol isomers
ρl	818.70	kg/m3	280.65	Temperature of maximum density for aqueous mixtures of three pentanol isomers
ρl	818.30	kg/m3	281.15	Temperature of maximum density for aqueous mixtures of three pentanol isomers
ρl	817.90	kg/m3	281.65	Temperature of maximum density for aqueous mixtures of three pentanol isomers
ρl	817.50	kg/m3	282.15	Temperature of maximum density for aqueous mixtures of three pentanol isomers
ρl	813.27	kg/m3	288.15	Volumetric properties of binary liquid mixtures of alcohols with 1,2-dichloroethane at different temperatures and atmospheric pressure
ρl	813.55	kg/m3	288.15	Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Pentanol, 2-Pentanol, or 2-Methyl-1-Butanol from (288.15 to 338.15) K at 0.1 MPa
ρl	813.34	kg/m3	288.15	Densities and Viscosities for Binary Liquid Mixtures of Pentanol Isomers from (288.15 to 328.15) K at 0.1 MPa
ρl	809.30	kg/m3	293.15	Thermodynamic and transport properties of binary mixtures; friction theory coupled with PC-SAFT model
ρl	810.10	kg/m3	293.15	Effect of 1-ethyl-3-methylimidazolium tetrafluoroborate on the phase equilibria for systems containing 5-hydroxymethylfurfural, water, organic solvent in the absence and presence of sodium chloride
ρl	809.30	kg/m3	293.15	Volumetric properties of binary liquid mixtures of alcohols with 1,2-dichloroethane at different temperatures and atmospheric pressure
ρl	809.59	kg/m3	293.15	Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Pentanol, 2-Pentanol, or 2-Methyl-1-Butanol from (288.15 to 338.15) K at 0.1 MPa
ρl	809.30	kg/m3	293.15	Evaluation of thermodynamic properties of fluid mixtures by PC-SAFT model
ρl	809.30	kg/m3	293.15	Studies on Thermodynamic and Transport Properties of Binary Mixtures Containing Alcohols and Aniline
ρl	809.38	kg/m3	293.15	Densities and Viscosities for Binary Liquid Mixtures of Pentanol Isomers from (288.15 to 328.15) K at 0.1 MPa
ρl	809.40	kg/m3	293.15	Acoustic, volumetric and spectral studies of binary liquid mixtures of aliphatic dialkylamine and 2-alkanols at different temperatures
ρl	809.30	kg/m3	293.15	Densities and Viscosities of Binary Mixtures Containing Ethyl Formate and 2-Alkanols: Friction Theory and Free Volume Theory
ρl	809.30	kg/m3	293.15	Influence of Temperature and Carbon Chain on Thermophysical Properties of Benzaldehyde/Alkan-2-ol Binary Mixtures
ρl	805.37	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	805.55	kg/m3	298.15	Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Pentanol, 2-Pentanol, or 2-Methyl-1-Butanol from (288.15 to 338.15) K at 0.1 MPa
ρl	805.40	kg/m3	298.15	Thermodynamic Properties of Binary Mixtures Containing N,N-Dimethylacetamide + 2-Alkanol: Experimental Data and Modeling
ρl	805.30	kg/m3	298.15	Thermodynamic and transport properties of binary mixtures; friction theory coupled with PC-SAFT model
ρl	805.30	kg/m3	298.15	Densities and Viscosities of Binary Mixtures Containing Ethyl Formate and 2-Alkanols: Friction Theory and Free Volume Theory
ρl	805.35	kg/m3	298.15	Densities and Viscosities for Binary Liquid Mixtures of Pentanol Isomers from (288.15 to 328.15) K at 0.1 MPa
ρl	806.11	kg/m3	298.15	Excess molar enthalpies of the binary systems: (Dibutyl ether + isomers of pentanol) at T = (298.15 and 308.15) K
ρl	805.37	kg/m3	298.15	Acoustic, volumetric and spectral studies of binary liquid mixtures of aliphatic dialkylamine and 2-alkanols at different temperatures
ρl	805.30	kg/m3	298.15	Evaluation of thermodynamic properties of fluid mixtures by PC-SAFT model
ρl	805.30	kg/m3	298.15	Studies on Thermodynamic and Transport Properties of Binary Mixtures Containing Alcohols and Aniline
ρl	806.48	kg/m3	298.15	Excess volumes and partial molar volumes of binary liquid mixtures of furfural or 2-methylfuran with alcohols at 298.15 K
ρl	805.30	kg/m3	298.15	Influence of Temperature and Carbon Chain on Thermophysical Properties of Benzaldehyde/Alkan-2-ol Binary Mixtures
ρl	806.57	kg/m3	298.15	Isobaric Vapor Liquid Equilibria of Binary Systems (Propyl Acetate + n-Pentanol), (Propyl Acetate + 1-Methyl-1-butanol), and (Propyl Acetate + 3-Methyl-1-butanol) at 101.3 kPa
ρl	805.27	kg/m3	298.15	Volumetric properties of binary liquid mixtures of alcohols with 1,2-dichloroethane at different temperatures and atmospheric pressure
ρl	805.05	kg/m3	298.15	Densities and viscosities of the mixtures (formamide + 2-alkanol): Experimental and theoretical approaches
ρl	805.37	kg/m3	298.20	Liquid-liquid equilibrium in systems used for the production of 5-hydroxymethylfurfural from biomass using alcohols as solvents
ρl	801.20	kg/m3	303.15	Evaluation of thermodynamic properties of fluid mixtures by PC-SAFT model
ρl	801.20	kg/m3	303.15	Influence of Temperature and Carbon Chain on Thermophysical Properties of Benzaldehyde/Alkan-2-ol Binary Mixtures
ρl	800.90	kg/m3	303.15	Thermodynamic Properties of Binary Mixtures Containing N,N-Dimethylacetamide + 2-Alkanol: Experimental Data and Modeling
ρl	801.16	kg/m3	303.15	Volumetric properties of binary liquid mixtures of alcohols with 1,2-dichloroethane at different temperatures and atmospheric pressure
ρl	801.24	kg/m3	303.15	Densities and Viscosities for Binary Liquid Mixtures of Pentanol Isomers from (288.15 to 328.15) K at 0.1 MPa
ρl	801.20	kg/m3	303.15	Thermodynamic and transport properties of binary mixtures; friction theory coupled with PC-SAFT model
ρl	800.88	kg/m3	303.15	Densities and viscosities of the mixtures (formamide + 2-alkanol): Experimental and theoretical approaches
ρl	801.44	kg/m3	303.15	Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Pentanol, 2-Pentanol, or 2-Methyl-1-Butanol from (288.15 to 338.15) K at 0.1 MPa
ρl	801.20	kg/m3	303.15	Densities and Viscosities of Binary Mixtures Containing Ethyl Formate and 2-Alkanols: Friction Theory and Free Volume Theory
ρl	801.27	kg/m3	303.15	Acoustic, volumetric and spectral studies of binary liquid mixtures of aliphatic dialkylamine and 2-alkanols at different temperatures
ρl	801.20	kg/m3	303.15	Studies on Thermodynamic and Transport Properties of Binary Mixtures Containing Alcohols and Aniline
ρl	797.00	kg/m3	308.15	Densities and Viscosities of Binary Mixtures Containing Ethyl Formate and 2-Alkanols: Friction Theory and Free Volume Theory
ρl	797.25	kg/m3	308.15	Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Pentanol, 2-Pentanol, or 2-Methyl-1-Butanol from (288.15 to 338.15) K at 0.1 MPa
ρl	796.97	kg/m3	308.15	Volumetric properties of binary liquid mixtures of alcohols with 1,2-dichloroethane at different temperatures and atmospheric pressure
ρl	797.05	kg/m3	308.15	Densities and Viscosities for Binary Liquid Mixtures of Pentanol Isomers from (288.15 to 328.15) K at 0.1 MPa
ρl	797.00	kg/m3	308.15	Evaluation of thermodynamic properties of fluid mixtures by PC-SAFT model
ρl	797.00	kg/m3	308.15	Thermodynamic and transport properties of binary mixtures; friction theory coupled with PC-SAFT model
ρl	797.00	kg/m3	308.15	Studies on Thermodynamic and Transport Properties of Binary Mixtures Containing Alcohols and Aniline
ρl	797.00	kg/m3	308.15	Influence of Temperature and Carbon Chain on Thermophysical Properties of Benzaldehyde/Alkan-2-ol Binary Mixtures
ρl	796.90	kg/m3	308.15	Thermodynamic Properties of Binary Mixtures Containing N,N-Dimethylacetamide + 2-Alkanol: Experimental Data and Modeling
ρl	796.89	kg/m3	308.15	Densities and viscosities of the mixtures (formamide + 2-alkanol): Experimental and theoretical approaches
ρl	798.00	kg/m3	308.15	Excess molar enthalpies of the binary systems: (Dibutyl ether + isomers of pentanol) at T = (298.15 and 308.15) K
ρl	796.95	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	797.08	kg/m3	308.15	Acoustic, volumetric and spectral studies of binary liquid mixtures of aliphatic dialkylamine and 2-alkanols at different temperatures
ρl	792.70	kg/m3	313.15	Influence of Temperature and Carbon Chain on Thermophysical Properties of Benzaldehyde/Alkan-2-ol Binary Mixtures
ρl	792.70	kg/m3	313.15	Volumetric properties of binary liquid mixtures of alcohols with 1,2-dichloroethane at different temperatures and atmospheric pressure
ρl	792.62	kg/m3	313.15	Densities and viscosities of the mixtures (formamide + 2-alkanol): Experimental and theoretical approaches
ρl	792.98	kg/m3	313.15	Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Pentanol, 2-Pentanol, or 2-Methyl-1-Butanol from (288.15 to 338.15) K at 0.1 MPa
ρl	792.78	kg/m3	313.15	Densities and Viscosities for Binary Liquid Mixtures of Pentanol Isomers from (288.15 to 328.15) K at 0.1 MPa
ρl	792.70	kg/m3	313.15	Densities and Viscosities of Binary Mixtures Containing Ethyl Formate and 2-Alkanols: Friction Theory and Free Volume Theory
ρl	792.70	kg/m3	313.15	Evaluation of thermodynamic properties of fluid mixtures by PC-SAFT model
ρl	792.60	kg/m3	313.15	Thermodynamic Properties of Binary Mixtures Containing N,N-Dimethylacetamide + 2-Alkanol: Experimental Data and Modeling
ρl	792.70	kg/m3	313.15	Studies on Thermodynamic and Transport Properties of Binary Mixtures Containing Alcohols and Aniline
ρl	792.70	kg/m3	313.15	Thermodynamic and transport properties of binary mixtures; friction theory coupled with PC-SAFT model
ρl	788.38	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	788.40	kg/m3	318.15	Influence of Temperature and Carbon Chain on Thermophysical Properties of Benzaldehyde/Alkan-2-ol Binary Mixtures
ρl	788.40	kg/m3	318.15	Evaluation of thermodynamic properties of fluid mixtures by PC-SAFT model
ρl	788.40	kg/m3	318.15	Densities and Viscosities of Binary Mixtures Containing Ethyl Formate and 2-Alkanols: Friction Theory and Free Volume Theory
ρl	788.63	kg/m3	318.15	Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Pentanol, 2-Pentanol, or 2-Methyl-1-Butanol from (288.15 to 338.15) K at 0.1 MPa
ρl	788.42	kg/m3	318.15	Densities and Viscosities for Binary Liquid Mixtures of Pentanol Isomers from (288.15 to 328.15) K at 0.1 MPa
ρl	788.40	kg/m3	318.15	Studies on Thermodynamic and Transport Properties of Binary Mixtures Containing Alcohols and Aniline
ρl	788.40	kg/m3	318.15	Thermodynamic and transport properties of binary mixtures; friction theory coupled with PC-SAFT model
ρl	784.00	kg/m3	323.15	Studies on Thermodynamic and Transport Properties of Binary Mixtures Containing Alcohols and Aniline
ρl	783.99	kg/m3	323.15	Densities and Viscosities for Binary Liquid Mixtures of Pentanol Isomers from (288.15 to 328.15) K at 0.1 MPa
ρl	784.19	kg/m3	323.15	Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Pentanol, 2-Pentanol, or 2-Methyl-1-Butanol from (288.15 to 338.15) K at 0.1 MPa
ρl	784.00	kg/m3	323.15	Thermodynamic and transport properties of binary mixtures; friction theory coupled with PC-SAFT model
ρl	784.00	kg/m3	323.15	Influence of Temperature and Carbon Chain on Thermophysical Properties of Benzaldehyde/Alkan-2-ol Binary Mixtures
ρl	784.00	kg/m3	323.15	Evaluation of thermodynamic properties of fluid mixtures by PC-SAFT model
ρl	784.00	kg/m3	323.15	Densities and Viscosities of Binary Mixtures Containing Ethyl Formate and 2-Alkanols: Friction Theory and Free Volume Theory
ρl	779.46	kg/m3	328.15	Densities and Viscosities for Binary Liquid Mixtures of Pentanol Isomers from (288.15 to 328.15) K at 0.1 MPa
ρl	779.67	kg/m3	328.15	Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Pentanol, 2-Pentanol, or 2-Methyl-1-Butanol from (288.15 to 338.15) K at 0.1 MPa
ρl	779.17	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
ρl	775.07	kg/m3	333.15	Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Pentanol, 2-Pentanol, or 2-Methyl-1-Butanol from (288.15 to 338.15) K at 0.1 MPa
ρl	770.37	kg/m3	338.15	Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Pentanol, 2-Pentanol, or 2-Methyl-1-Butanol from (288.15 to 338.15) K at 0.1 MPa
csound,fluid	[1168.10; 1286.70]	m/s	[283.15; 313.15]
csound,fluid	1286.70	m/s	283.15	Excess Molar Enthalpy, Density, and Speed of Sound for the Mixtures a-Pinene + 1- or 2-Pentanol at (283.15, 298.15, and 313.15) K
csound,fluid	1232.60	m/s	298.15	Excess Molar Enthalpy, Density, and Speed of Sound for the Mixtures a-Pinene + 1- or 2-Pentanol at (283.15, 298.15, and 313.15) K
csound,fluid	1168.10	m/s	313.15	Excess Molar Enthalpy, Density, and Speed of Sound for the Mixtures a-Pinene + 1- or 2-Pentanol at (283.15, 298.15, and 313.15) K
γ	[0.02; 0.02]	N/m	[293.15; 323.15]
γ	0.02	N/m	293.15	Surface Tension of Dilute Solutions of Linear Alcohols in Benzyl Alcohol
γ	0.02	N/m	298.15	Surface Tension of Dilute Solutions of Linear Alcohols in Benzyl Alcohol
γ	0.02	N/m	303.15	Surface Tension of Dilute Solutions of Linear Alcohols in Benzyl Alcohol
γ	0.02	N/m	308.15	Surface Tension of Dilute Solutions of Linear Alcohols in Benzyl Alcohol
γ	0.02	N/m	313.15	Surface Tension of Dilute Solutions of Linear Alcohols in Benzyl Alcohol
γ	0.02	N/m	318.15	Surface Tension of Dilute Solutions of Linear Alcohols in Benzyl Alcohol
γ	0.02	N/m	323.15	Surface Tension of Dilute Solutions of Linear Alcohols in Benzyl Alcohol

Datasets

Isobaric coefficient of expansion, 1/K

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Isobaric coefficient of expansion, 1/K - Liquid
278.15	5000.00	0.0009
278.15	10000.00	0.0009
278.15	15000.00	0.0008
278.15	20000.00	0.0008
278.15	25000.00	0.0008
278.15	30000.00	0.0008
278.15	35000.00	0.0008
278.15	40000.00	0.0008
278.15	45000.00	0.0007
278.15	50000.00	0.0007
278.15	55000.00	0.0007
288.15	5000.00	0.0009
288.15	10000.00	0.0009
288.15	15000.00	0.0009
288.15	20000.00	0.0009
288.15	25000.00	0.0008
288.15	30000.00	0.0008
288.15	35000.00	0.0008
288.15	40000.00	0.0008
288.15	45000.00	0.0008
288.15	50000.00	0.0008
288.15	55000.00	0.0007
298.15	5000.00	0.0010
298.15	10000.00	0.0009
298.15	15000.00	0.0009
298.15	20000.00	0.0009
298.15	25000.00	0.0009
298.15	30000.00	0.0009
298.15	35000.00	0.0008
298.15	40000.00	0.0008
298.15	45000.00	0.0008
298.15	50000.00	0.0008
298.15	55000.00	0.0008
308.15	5000.00	0.0010
308.15	10000.00	0.0010
308.15	15000.00	0.0010
308.15	20000.00	0.0009
308.15	25000.00	0.0009
308.15	30000.00	0.0009
308.15	35000.00	0.0009
308.15	40000.00	0.0008
308.15	45000.00	0.0008
308.15	50000.00	0.0008
308.15	55000.00	0.0008
318.15	5000.00	0.0011
318.15	10000.00	0.0010
318.15	15000.00	0.0010
318.15	20000.00	0.0010
318.15	25000.00	0.0009
318.15	30000.00	0.0009
318.15	35000.00	0.0009
318.15	40000.00	0.0009
318.15	45000.00	0.0009
318.15	50000.00	0.0008
318.15	55000.00	0.0008
328.15	5000.00	0.0011
328.15	10000.00	0.0011
328.15	15000.00	0.0010
328.15	20000.00	0.0010
328.15	25000.00	0.0010
328.15	30000.00	0.0010
328.15	35000.00	0.0009
328.15	40000.00	0.0009
328.15	45000.00	0.0009
328.15	50000.00	0.0009
328.15	55000.00	0.0008
338.15	5000.00	0.0011
338.15	10000.00	0.0011
338.15	15000.00	0.0011
338.15	20000.00	0.0010
338.15	25000.00	0.0010
338.15	30000.00	0.0010
338.15	35000.00	0.0010
338.15	40000.00	0.0009
338.15	45000.00	0.0009
338.15	50000.00	0.0009
338.15	55000.00	0.0009
348.15	5000.00	0.0012
348.15	10000.00	0.0011
348.15	15000.00	0.0011
348.15	20000.00	0.0011
348.15	25000.00	0.0010
348.15	30000.00	0.0010
348.15	35000.00	0.0010
348.15	40000.00	0.0010
348.15	45000.00	0.0009
348.15	50000.00	0.0009
348.15	55000.00	0.0009
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[123.74; 296.49]	J/mol×K	[273.00; 1000.00]	Joback Predicted correlation
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K
Coefficient A			1.95200e+00
Coefficient B			5.18740e-01
Coefficient C			-2.81800e-04
Coefficient D			5.76000e-08
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	123.74	J/mol×K	273.00	Calculated Property
Cp,gas	152.75	J/mol×K	353.78	Calculated Property
Cp,gas	178.89	J/mol×K	434.56	Calculated Property
Cp,gas	202.32	J/mol×K	515.33	Calculated Property
Cp,gas	223.24	J/mol×K	596.11	Calculated Property
Cp,gas	241.83	J/mol×K	676.89	Calculated Property
Cp,gas	258.27	J/mol×K	757.67	Calculated Property
Cp,gas	272.73	J/mol×K	838.44	Calculated Property
Cp,gas	285.42	J/mol×K	919.22	Calculated Property
Cp,gas	296.49	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.67]	kPa	[304.46; 413.88]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.42610e+01
Coefficient B			-2.72373e+03
Coefficient C			-1.09535e+02
Temperature range, min.			304.46
Temperature range, max.			413.88
Pvap	1.33	kPa	304.46	Calculated Property
Pvap	3.03	kPa	316.62	Calculated Property
Pvap	6.28	kPa	328.78	Calculated Property
Pvap	12.07	kPa	340.93	Calculated Property
Pvap	21.71	kPa	353.09	Calculated Property
Pvap	36.95	kPa	365.25	Calculated Property
Pvap	59.92	kPa	377.41	Calculated Property
Pvap	93.17	kPa	389.56	Calculated Property
Pvap	139.66	kPa	401.72	Calculated Property
Pvap	202.67	kPa	413.88	Calculated Property
Pvap	[5.64e-06; 3752.61]	kPa	[200.00; 552.00]	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			1.30709e+02
Coefficient B			-1.10289e+04
Coefficient C			-1.66000e+01
Coefficient D			7.56865e-06
Coefficient E			0.00000e+00
Temperature range, min.			200.00
Temperature range, max.			552.00
Pvap	5.64e-06	kPa	200.00	Calculated Property
Pvap	2.74e-03	kPa	239.11	Calculated Property
Pvap	0.17	kPa	278.22	Calculated Property
Pvap	3.01	kPa	317.33	Calculated Property
Pvap	24.15	kPa	356.44	Calculated Property
Pvap	114.22	kPa	395.56	Calculated Property
Pvap	375.23	kPa	434.67	Calculated Property
Pvap	954.14	kPa	473.78	Calculated Property
Pvap	2020.91	kPa	512.89	Calculated Property
Pvap	3752.61	kPa	552.00	Calculated Property
Pvap	[0.80; 73.47]	kPa	[298.12; 383.34]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.47906e+01
Coefficient B			-2.97313e+03
Coefficient C			-1.00017e+02
Reference			Butler, Ramchandani, et al., 1935, 2
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			298.12
Temperature range, max.			383.34
Pvap	0.80	kPa	298.12	Calculated Property
Pvap	1.60	kPa	307.59	Calculated Property
Pvap	2.98	kPa	317.06	Calculated Property
Pvap	5.28	kPa	326.53	Calculated Property
Pvap	8.95	kPa	336.00	Calculated Property
Pvap	14.55	kPa	345.46	Calculated Property
Pvap	22.82	kPa	354.93	Calculated Property
Pvap	34.65	kPa	364.40	Calculated Property
Pvap	51.11	kPa	373.87	Calculated Property
Pvap	73.47	kPa	383.34	Calculated Property
Pvap	[0.80; 73.47]	kPa	[298.12; 383.34]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.47906e+01
Coefficient B			-2.97313e+03
Coefficient C			-1.00017e+02
Reference			Butler, Ramchandani, et al., 1935
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			298.12
Temperature range, max.			383.34
Pvap	0.80	kPa	298.12	Calculated Property
Pvap	1.60	kPa	307.59	Calculated Property
Pvap	2.98	kPa	317.06	Calculated Property
Pvap	5.28	kPa	326.53	Calculated Property
Pvap	8.95	kPa	336.00	Calculated Property
Pvap	14.55	kPa	345.46	Calculated Property
Pvap	22.82	kPa	354.93	Calculated Property
Pvap	34.65	kPa	364.40	Calculated Property
Pvap	51.11	kPa	373.87	Calculated Property
Pvap	73.47	kPa	383.34	Calculated Property

Similar Compounds

Find more compounds similar to 2-Pentanol.

Mixtures

• 2-Pentanol + Water
• 2-Pentanol + Sodium nitrate + Water
• Potassium nitrate + 2-Pentanol + Water
• n-Hexane + 2-Pentanol
• 2-Pentanol + Cyclohexanamine, N-methyl-
• Carbon dioxide + 2-Pentanol
• 2-Pentanol + Cyclohexane, methyl-
• Propanal + 2-Pentanol
• 2-Pentanol + 2-Butene, (Z)-
• 2-Pentanol + Dimethyl ether
• Ethyl Chloride + 2-Pentanol
• 2-Pentanol + Ethane, 1,1-difluoro-
• Acetonitrile + 2-Pentanol
• 2-Pentanol + Ethanamine, N-ethyl-
• 2-Pentanol + Cyclohexane
• Toluene + 2-Pentanol
• 2-Pentanol + Water + Phosphoric Acid
• 5-Hydroxymethylfurfural + 2-Pentanol + Water
• Propane + 2-Pentanol
• Propene + 2-Pentanol

Find more mixtures with 2-Pentanol.

Sources

• KDB Vapor Pressure Data
• Cheméo Relay (1.0)
• Crippen Method
• Vapor liquid equilibria for nitrogen with 2-propanol, 2-butanol, or 2-pentanol binary systems
• Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
• The influence of cation, anion and temperature on the liquid-liquid equilibrium of some pentanols-water system
• Thermodynamic behaviour of second generation biofuels: Vapour liquid equilibria and excess enthalpies of the binary mixtures 2-pentanol and n-heptane or 2,2,4-trimethylpentane
• Thermodynamics properties, VLE and HE, of the systems 2-pentanol and cyclohexane or methylbenzene for contributing to the knowledge of new biofuels
• Characterizing second generation biofuels: Excess enthalpies and vapour-liquid equilibria of the binary mixtures containing 1-pentanol or 2-pentanol and n-hexane
• Vapor-liquid equilibria and excess enthalpies of the binary systems 1- pentanol or 2-pentanol and 1-hexene or 1,2,4-trimethylbenzene for the development of biofuels
• Solubility of 1-methyl-4-nitropyrazole in seventeen pure solvents at temperatures from 283.15 K to 323.15 K
• Liquid-liquid equilibria of ternary and quaternary systems involving 5-hydroxymethylfurfural, water, organic solvents, and salts at 313.15 K and atmospheric pressure
• A thermodynamic study of the ketoreductase-catalyzed reduction of 2-alkanones in non-aqueous solvents
• Henry's constants and infinite dilution activity coefficients of propane, propene, butane, isobutane, 1-butene, isobutene, trans-2-butene, and 1,3-butadiene in 1-pentanol, 2-pentanol and 3-pentanol
• Speeds of sound, isentropic compressibilities, viscosities and excess molar volumes of binary mixtures of methylcyclohexane + 2-alkanols or ethanol at T = 298.15 K
• Henry's law constants and infinite dilution activity coefficients of cis-2-butene, dimethylether, chloroethane, and 1,1-difluoroethane in methanol, 1-propanol, 2-propanol, 1-butanol, 2-butanol, isobutanol, tert-butanol, 1-pentanol, 2-pentanol, 3-pentanol, 2-methyl-1-butanol, 3-methyl-1-butanol, and 2-methyl-2-butanol
• Viscosity, density, and speed of sound of methylcyclopentane with primary and secondary alcohols at T = (293.15, 298.15, and 303.15) K
• Isobaric thermal expansivity behaviour against temperature and pressure of associating fluids
• Measurement and modeling of high-pressure (vapor + liquid) equilibria of (CO2 + alkanol) binary systems
• Densities and viscosities of the mixtures (formamide + 2-alkanol): Experimental and theoretical approaches
• Excess molar enthalpies of the binary systems: (Dibutyl ether + isomers of pentanol) at T = (298.15 and 308.15) K
• Thermodynamic and transport properties of binary mixtures; friction theory coupled with PC-SAFT model
• Liquid-liquid equilibria for ternary mixtures of 1-alkyl-3-methyl imidazolium bis{(trifluoromethyl)sulfonyl}imides, n-hexane and organic compounds at 303.15 K and 0.1 MPa
• The study of physico-chemical properties of binary systems consisting of N-Methylcyclohexylamine with 2-alkanols at T = (298.15-328.15) K
• Liquid-liquid equilibrium in systems used for the production of 5-hydroxymethylfurfural from biomass using alcohols as solvents
• Studies on physicochemical behavior of binary mixtures containing propanal and Alkan-2-ol
• Temperature of maximum density for aqueous mixtures of three pentanol isomers
• Phase equilibria of the water + 1-butanol + 2-pentanol ternary system at 101.3 kPa
• Acoustic, volumetric and spectral studies of binary liquid mixtures of aliphatic dialkylamine and 2-alkanols at different temperatures
• Effect of 1-ethyl-3-methylimidazolium tetrafluoroborate on the phase equilibria for systems containing 5-hydroxymethylfurfural, water, organic solvent in the absence and presence of sodium chloride
• Excess volumes and partial molar volumes of binary liquid mixtures of furfural or 2-methylfuran with alcohols at 298.15 K
• Experimental and modeling study of liquid phase equilibria for (water + phosphoric acid + sec-alcohols) systems
• Thermophysical study of binary mixtures of 1-butyl-3-methylimidazolium nitrate ionic liquid + alcohols at different temperatures
• Solution enthalpies of 1-bromoadamantane in monoalcohols at 298.15K
• 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
• Volumetric properties of binary liquid mixtures of alcohols with 1,2-dichloroethane at different temperatures and atmospheric pressure
• Densities and viscosities of binary mixtures of ethylmethylketone and 2-alkanols; application of the ERAS model and cubic EOS
• Evaluation of thermodynamic properties of fluid mixtures by PC-SAFT model
• Studies on Thermodynamic and Transport Properties of Binary Mixtures Containing Alcohols and Aniline
• Influence of Temperature and Carbon Chain on Thermophysical Properties of Benzaldehyde/Alkan-2-ol Binary Mixtures
• Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Pentanol, 2-Pentanol, or 2-Methyl-1-Butanol from (288.15 to 338.15) K at 0.1 MPa
• Densities and Viscosities for Binary Liquid Mixtures of Pentanol Isomers from (288.15 to 328.15) K at 0.1 MPa
• Solubility in Binary Solvent Mixtures: Anthracene Dissolved in Alcohol + Acetonitrile Mixtures at 298.2 K
• Solubility in Binary Solvent Mixtures: Pyrene Dissolved in Alcohol + Acetonitrile Mixtures at 299.2 K
• Solubility in Binary Solvent Mixtures: Anthracene Dissolved in Alcohol + 2-Methyl-1-butanol Mixtures at 298.2 K
• Dynamic Viscosities of 2-Pentanol with Alkanes (Octane, Decane, and Dodecane) at Three Temperatures T ) (293.15, 298.15, and 303.15) K. New UNIFAC-VISCO Interaction Parameters
• Partial Molar Heat Capacities and Partial Molar Volumes of All of the Isomeric (C3 to C5) Alkanols at Infinite Dilution in Water at 298.15 K
• Surface Tension of Dilute Solutions of Linear Alcohols in Benzyl Alcohol
• Measurement and Correlation of Vapor-Liquid Equilibria for Water + 2-Propanol, Water + 2-Butanol, and Water + 2-Pentanol Systems at High Temperatures and Pressures
• Viscosities, Densities, and Speed of Sound of the Cycloalkanes with Secondary Alcohols at T = (293.15, 298.15, and 303.15) K: New UNIFAC-VISCO Interaction Parameters
• Excess Molar Enthalpy, Density, and Speed of Sound for the Mixtures a-Pinene + 1- or 2-Pentanol at (283.15, 298.15, and 313.15) K
• Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
• Densities and Viscosities of Binary Mixtures of Cyclohexanone and 2-Alkanols
• Densities and Viscosities of Binary Mixtures Containing Diethylene Glycol and 2-Alkanol
• Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
• Isobaric Vapor Liquid Equilibria of Binary Systems (Propyl Acetate + n-Pentanol), (Propyl Acetate + 1-Methyl-1-butanol), and (Propyl Acetate + 3-Methyl-1-butanol) at 101.3 kPa
• Thermodynamic Properties of Binary Mixtures Containing N,N-Dimethylacetamide + 2-Alkanol: Experimental Data and Modeling
• Densities and Viscosities of Binary Mixtures Containing Ethyl Formate and 2-Alkanols: Friction Theory and Free Volume Theory
• Refined Flow Microcalorimetric Setup for Measurement of Mixing Enthalpies at High Dilutions: Determination of Infinite Dilution Dissolution Enthalpies of Some Alkanol and Ether Solutes in Water
• Measurement of Infinite Dilution Activity Coefficients of Alcohols, Ketones, and Aromatic Hydrocarbons in 4-Methyl-N-butylpyridinium Tetrafluoroborate and 1-Butyl-3-methylimidazolium Hexafluorophosphate by Gas-Liquid Chromatography
• Solubility of D(-)-p-Hydroxyphenylglycine Dane Salt in Eight Alcohols between (293 and 343) K
• Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
• Vapor-Liquid Equilibria in Binary Systems Formed by n-Hexane with Alcohols
• Densities, Viscosities, and Refractive Indices of Binary Mixtures of Acetophenone and 2-Alkanols
• Temperature Dependence of Limiting Activity Coefficients, Henry s Law Constants, and Related Infinite Dilution Properties of Branched Pentanols in Water. Measurement, Critical Compilation, Correlation, and Recommended Data
• Densities, Viscosities, and Refractive Indices of Binary Mixtures of Methyl Ethyl Ketone + Pentanol Isomers at Different Temperatures
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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