Chemical Properties of 1-Heptanol (CAS 111-70-6)

InChI

InChI=1S/C7H16O/c1-2-3-4-5-6-7-8/h8H,2-7H2,1H3

InChI Key

BBMCTIGTTCKYKF-UHFFFAOYSA-N

Formula

C7H16O

SMILES

CCCCCCCO

Molecular Weight¹

116.20

CAS

111-70-6

Other Names

• 1-HeptanoI
• 1-Heptyl alcohol
• 1-hydroxyheptane
• Alcohol C7
• Enanthic alcohol
• Enanthyl alcohol
• Gentanol
• Heptane-1-ol
• Heptanol-1
• Heptyl alcohol, n-
• NSC 3703
• heptan-1-ol
• heptyl alcohol
• hexylcarbinol
• l'Alcool n-heptylique primaire
• n-C7H15OH
• n-Heptan-1-ol
• n-Heptanol
• n-Heptanol-1
• n-heptyl alcohol

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• T_ig : Autoignition Temperature (K).
• 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).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• T_flash,cc : Flash Point (Closed Cup Method) (K).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• ν : Kinematic viscosity (m²/s).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_c : Critical density (kg/m³).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I_p : Polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_gas : Molar entropy at standard conditions (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• c_sound,fluid : Speed of sound in fluid (m/s).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_boilr : Boiling point at reduced pressure (K).
• T_c : Critical Temperature (K).
• λ_gas : Gas thermal conductivity (W/m×K).
• λ_liquid : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• U_Qi : UNIQUAC Qi Parameter.
• U_Ri : UNIQUAC Ri Parameter.
• V_c : Critical Volume (m³/kmol).
• Z_c : Critical Compressibility.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Contents

1. Physical Properties
2. Temperature Dependent Properties
3. Pressure Dependent Properties
4. Datasets
5. Correlations
6. Similar Compounds
7. Mixtures
8. Sources

Physical Properties

Property	Value	Unit	Source
ω	[0.5600; 0.5820]
ω	0.5600		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.5820		ChemSep v8.3 pure component data Compiled value
ω	0.5600		KDB
PAff	799.00	kJ/mol	NIST
Tig	255.37	K	KDB
ΔcH°liquid	[-4642.52; -4631.90]	kJ/mol
ΔcH°liquid	-4637.80 ± 0.50	kJ/mol	NIST
ΔcH°liquid	-4638.01 ± 0.79	kJ/mol	NIST
ΔcH°liquid	-4642.52 ± 0.71	kJ/mol	NIST
ΔcH°liquid	-4631.90 ± 2.30	kJ/mol	NIST
ΔcH°liquid	-4631.90	kJ/mol	NIST
μ	[1.67; 1.70]	debye
μ	1.67	debye	ChemSep v8.3 pure component data Compiled value
μ	1.70	debye	KDB
Tflash,cc	[349.82; 350.15]	K
Tflash,cc	349.82	K	KDB
Tflash,cc	350.15	K	NCMS SOLV-DB
ΔfG°	[-125.30; -121.00]	kJ/mol
ΔfG°	-125.30	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	-121.00	kJ/mol	KDB
ΔfH°gas	[-393.60; -329.10]	kJ/mol
ΔfH°gas	-332.00	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-332.00	kJ/mol	KDB
ΔfH°gas	-333.70	kJ/mol	NIST
ΔfH°gas	-336.60 ± 0.50	kJ/mol	NIST
ΔfH°gas	-336.40 ± 0.80	kJ/mol	NIST
ΔfH°gas	-329.10	kJ/mol	NIST
ΔfH°gas	-332.00 ± 0.90	kJ/mol	NIST
ΔfH°gas	-339.70 ± 1.60	kJ/mol	NIST
ΔfH°gas	Outlier -393.60 ± 3.00	kJ/mol	NIST
ΔfH°liquid	[-460.40; -398.80]	kJ/mol
ΔfH°liquid	-403.40 ± 0.50	kJ/mol	NIST
ΔfH°liquid	-403.20 ± 0.80	kJ/mol	NIST
ΔfH°liquid	-398.80 ± 0.84	kJ/mol	NIST
ΔfH°liquid	-409.40 ± 2.30	kJ/mol	NIST
ΔfH°liquid	-460.40 ± 3.00	kJ/mol	NIST
ΔfusH°	18.35	kJ/mol	Heat Capacities and Derived Thermodynamic Functions of 1-Hexanol, 1-Heptanol, 1-Octanol, and 1-Decanol between 5 K and 390 K
ΔvapH°	[4.48; 69.70]	kJ/mol
ΔvapH°	Outlier 4.48	kJ/mol	NCMS SOLV-DB
ΔvapH°	66.81	kJ/mol	NIST
ΔvapH°	67.10	kJ/mol	NIST
ΔvapH°	66.90 ± 0.40	kJ/mol	NIST
ΔvapH°	66.50	kJ/mol	NIST
ΔvapH°	66.40	kJ/mol	NIST
ΔvapH°	66.81 ± 0.20	kJ/mol	NIST
ΔvapH°	66.80 ± 0.20	kJ/mol	NIST
ΔvapH°	67.80 ± 1.50	kJ/mol	NIST
ΔvapH°	69.70	kJ/mol	NIST
IE	[9.84; 10.40]	eV
IE	10.40 ± 0.10	eV	NIST
IE	9.84	eV	NIST
IE	10.35	eV	NIST
log10WS	[-1.81; -1.81]
log10WS	-1.81		Aq. Solubility Prediction
log10WS	-1.81		Estimated Solubility
logPoct/wat	2.410		NCMS SOLV-DB
McVol	115.360	ml/mol	McGowan Calculated Property
Pc	[3039.75; 3160.00]	kPa
Pc	3058.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 Compiled value
Pc	3039.75	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	3150.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	3058.00	kPa	KDB
Pc	3060.00 ± 20.00	kPa	NIST
Pc	3160.00 ± 50.00	kPa	NIST
Pc	3058.00 ± 20.00	kPa	NIST
Pc	3058.00 ± 20.00	kPa	NIST
Ptriple	1.18e-05	kPa	ChemSep v8.3 pure component data Compiled value
ρc	[266.10; 267.26]	kg/m3
ρc	267.26 ± 2.32	kg/m3	NIST
ρc	267.26	kg/m3	NIST
ρc	266.10 ± 27.89	kg/m3	NIST
ρc	267.26 ± 3.49	kg/m3	NIST
Inp	[154.52; 989.00]
Inp	942.00		NIST
Inp	951.60		NIST
Inp	933.20		NIST
Inp	939.60		NIST
Inp	954.90		NIST
Inp	952.80		NIST
Inp	971.10		NIST
Inp	969.20		NIST
Inp	981.00		NIST
Inp	950.00		NIST
Inp	951.00		NIST
Inp	950.00		NIST
Inp	938.00		NIST
Inp	966.00		NIST
Inp	960.00		NIST
Inp	955.00		NIST
Inp	955.00		NIST
Inp	953.00		NIST
Inp	932.00		NIST
Inp	942.00		NIST
Inp	960.00		NIST
Inp	958.00		NIST
Inp	956.00		NIST
Inp	945.00		NIST
Inp	955.00		NIST
Inp	972.00		NIST
Inp	972.00		NIST
Inp	972.00		NIST
Inp	959.00		NIST
Inp	961.00		NIST
Inp	960.00		NIST
Inp	970.00		NIST
Inp	970.00		NIST
Inp	971.00		NIST
Inp	973.00		NIST
Inp	969.00		NIST
Inp	969.00		NIST
Inp	975.00		NIST
Inp	970.00		NIST
Inp	951.80		NIST
Inp	966.70		NIST
Inp	963.00		NIST
Inp	958.00		NIST
Inp	959.00		NIST
Inp	960.00		NIST
Inp	949.00		NIST
Inp	968.00		NIST
Inp	971.00		NIST
Inp	952.20		NIST
Inp	953.30		NIST
Inp	970.60		NIST
Inp	954.00		NIST
Inp	974.00		NIST
Inp	949.00		NIST
Inp	953.20		NIST
Inp	967.00		NIST
Inp	951.00		NIST
Inp	950.00		NIST
Inp	953.00		NIST
Inp	956.00		NIST
Inp	977.20		NIST
Inp	962.00		NIST
Inp	969.00		NIST
Inp	974.00		NIST
Inp	978.00		NIST
Inp	984.00		NIST
Inp	969.00		NIST
Inp	974.00		NIST
Inp	974.00		NIST
Inp	950.00		NIST
Inp	953.00		NIST
Inp	951.00		NIST
Inp	960.00		NIST
Inp	960.00		NIST
Inp	969.00		NIST
Inp	973.00		NIST
Inp	977.00		NIST
Inp	975.00		NIST
Inp	967.00		NIST
Inp	976.00		NIST
Inp	970.00		NIST
Inp	953.00		NIST
Inp	989.00		NIST
Inp	971.00		NIST
Inp	969.00		NIST
Inp	971.00		NIST
Inp	970.00		NIST
Inp	974.00		NIST
Inp	969.00		NIST
Inp	952.00		NIST
Inp	951.00		NIST
Inp	972.00		NIST
Inp	957.00		NIST
Inp	978.00		NIST
Inp	972.00		NIST
Inp	957.00		NIST
Inp	952.20		NIST
Inp	952.00		NIST
Inp	952.40		NIST
Inp	952.90		NIST
Inp	956.40		NIST
Inp	951.00		NIST
Inp	955.00		NIST
Inp	953.00		NIST
Inp	951.00		NIST
Inp	960.00		NIST
Inp	973.00		NIST
Inp	970.00		NIST
Inp	970.00		NIST
Inp	975.00		NIST
Inp	967.00		NIST
Inp	983.00		NIST
Inp	970.00		NIST
Inp	946.00		NIST
Inp	974.00		NIST
Inp	970.00		NIST
Inp	972.00		NIST
Inp	968.00		NIST
Inp	961.00		NIST
Inp	969.00		NIST
Inp	964.00		NIST
Inp	969.00		NIST
Inp	947.00		NIST
Inp	969.00		NIST
Inp	960.00		NIST
Inp	970.00		NIST
Inp	953.00		NIST
Inp	953.00		NIST
Inp	955.00		NIST
Inp	970.00		NIST
Inp	968.40		NIST
Inp	947.00		NIST
Inp	978.00		NIST
Inp	953.00		NIST
Inp	957.00		NIST
Inp	957.00		NIST
Inp	953.00		NIST
Inp	955.00		NIST
Inp	980.00		NIST
Inp	951.00		NIST
Inp	967.00		NIST
Inp	953.00		NIST
Inp	955.00		NIST
Inp	973.00		NIST
Inp	980.00		NIST
Inp	Outlier 154.52		NIST
Inp	Outlier 157.77		NIST
Inp	Outlier 155.86		NIST
Inp	977.20		NIST
Inp	984.00		NIST
Inp	970.00		NIST
Inp	969.00		NIST
Inp	963.00		NIST
Inp	968.00		NIST
Inp	954.00		NIST
Inp	951.00		NIST
Inp	972.00		NIST
Ip	[1405.00; 1471.00]
Ip	1456.00		NIST
Ip	Outlier 1405.00		NIST
Ip	1468.00		NIST
Ip	1427.00		NIST
Ip	1453.00		NIST
Ip	1427.00		NIST
Ip	1459.00		NIST
Ip	1467.00		NIST
Ip	1444.00		NIST
Ip	1461.00		NIST
Ip	1452.00		NIST
Ip	1431.00		NIST
Ip	1425.00		NIST
Ip	1460.00		NIST
Ip	1450.00		NIST
Ip	1423.00		NIST
Ip	1437.00		NIST
Ip	1450.00		NIST
Ip	1452.00		NIST
Ip	1461.00		NIST
Ip	1462.00		NIST
Ip	1441.00		NIST
Ip	1460.00		NIST
Ip	1463.00		NIST
Ip	1465.00		NIST
Ip	1462.00		NIST
Ip	1447.00		NIST
Ip	1446.00		NIST
Ip	1439.00		NIST
Ip	1452.00		NIST
Ip	1459.00		NIST
Ip	1439.00		NIST
Ip	1439.00		NIST
Ip	1456.00		NIST
Ip	1456.00		NIST
Ip	1443.00		NIST
Ip	1457.00		NIST
Ip	1460.00		NIST
Ip	1439.00		NIST
Ip	1470.00		NIST
Ip	1450.00		NIST
Ip	1457.00		NIST
Ip	Outlier 1421.00		NIST
Ip	1440.00		NIST
Ip	1440.00		NIST
Ip	1455.00		NIST
Ip	1440.00		NIST
Ip	1440.00		NIST
Ip	1458.00		NIST
Ip	1441.00		NIST
Ip	1460.00		NIST
Ip	1462.00		NIST
Ip	1463.00		NIST
Ip	1445.70		NIST
Ip	1452.90		NIST
Ip	1450.30		NIST
Ip	1447.40		NIST
Ip	1449.80		NIST
Ip	1449.30		NIST
Ip	1449.20		NIST
Ip	1448.40		NIST
Ip	1424.00		NIST
Ip	1460.00		NIST
Ip	1439.00		NIST
Ip	1444.00		NIST
Ip	1447.00		NIST
Ip	1459.00		NIST
Ip	1457.00		NIST
Ip	1449.00		NIST
Ip	1440.00		NIST
Ip	1468.00		NIST
Ip	1458.00		NIST
Ip	1464.00		NIST
Ip	1443.00		NIST
Ip	1458.00		NIST
Ip	1471.00		NIST
Ip	1457.00		NIST
Ip	1449.00		NIST
Ip	1462.00		NIST
Ip	1459.00		NIST
Ip	1454.00		NIST
Ip	1455.00		NIST
Ip	1462.00		NIST
Ip	1453.00		NIST
Ip	1457.00		NIST
Ip	1439.00		NIST
Ip	1463.00		NIST
Ip	1467.00		NIST
Ip	1452.00		NIST
Ip	1467.00		NIST
Ip	Outlier 1419.00		NIST
Ip	Outlier 1419.00		NIST
Ip	1458.00		NIST
Ip	1456.00		NIST
Ip	1460.00		NIST
Ip	1460.00		NIST
Ip	1467.00		NIST
Ip	1470.00		NIST
Ip	1456.00		NIST
Ip	1439.00		NIST
Ip	1450.00		NIST
Ip	1436.00		NIST
Ip	1440.00		NIST
Ip	1462.00		NIST
Ip	1460.00		NIST
Ip	1453.00		NIST
Ip	1429.00		NIST
Ip	1463.00		NIST
Ip	1468.00		NIST
Ip	1454.00		NIST
Ip	1459.00		NIST
Ip	1467.00		NIST
Ip	Outlier 1419.00		NIST
Ip	1452.00		NIST
Ip	1440.00		NIST
Ip	1470.00		NIST
Ip	1455.00		NIST
Ip	Outlier 1419.00		NIST
Ip	1449.00		NIST
Ip	1450.00		NIST
Ip	1430.00		NIST
Ip	1441.00		NIST
Ip	1460.00		NIST
Ip	1456.00		NIST
Ip	1427.00		NIST
Ip	1452.00		NIST
Ip	1423.00		NIST
Ip	1467.00		NIST
Ip	1436.00		NIST
Ip	1429.00		NIST
Ip	1455.00		NIST
Ip	1441.00		NIST
S°gas	485.80 ± 4.20	J/mol×K	NIST
S°liquid	325.90	J/mol×K	NIST
Tboil	[445.90; 450.15]	K
Tboil	449.52	K	Vapor-liquid equilibrium data of binary mixtures of 1-hexanol, 1-heptanol, 1-nonanol and 1,3-propanediol at P = 101.3 kPa using differential scanning calorimetry (DSC)
Tboil	449.81	K	ChemSep v8.3 pure component data Compiled value
Tboil	449.60	K	KDB
Tboil	449.15	K	NCMS SOLV-DB
Tboil	449.50	K	NIST
Tboil	447.30 ± 0.15	K	NIST
Tboil	449.55 ± 0.40	K	NIST
Tboil	Outlier 446.15 ± 2.00	K	NIST
Tboil	448.15 ± 2.00	K	NIST
Tboil	449.55 ± 1.00	K	NIST
Tboil	449.15 ± 2.00	K	NIST
Tboil	449.25 ± 0.50	K	NIST
Tboil	449.05 ± 0.50	K	NIST
Tboil	449.15 ± 0.50	K	NIST
Tboil	449.30 ± 0.50	K	NIST
Tboil	448.55 ± 0.30	K	NIST
Tboil	447.20 ± 0.60	K	NIST
Tboil	449.65 ± 2.00	K	NIST
Tboil	448.70 ± 0.60	K	NIST
Tboil	449.30 ± 0.20	K	NIST
Tboil	447.15 ± 2.00	K	NIST
Tboil	447.90 ± 2.00	K	NIST
Tboil	447.65 ± 3.00	K	NIST
Tboil	449.96 ± 0.40	K	NIST
Tboil	448.75 ± 0.35	K	NIST
Tboil	449.45 ± 0.50	K	NIST
Tboil	449.50 ± 0.20	K	NIST
Tboil	449.30 ± 0.30	K	NIST
Tboil	448.55 ± 2.00	K	NIST
Tboil	448.15 ± 2.00	K	NIST
Tboil	449.15 ± 0.50	K	NIST
Tboil	448.15 ± 2.00	K	NIST
Tboil	447.20 ± 0.40	K	NIST
Tboil	449.15 ± 3.00	K	NIST
Tboil	447.90 ± 1.00	K	NIST
Tboil	449.15 ± 2.00	K	NIST
Tboil	447.65 ± 2.00	K	NIST
Tboil	Outlier 446.15 ± 1.00	K	NIST
Tboil	448.15 ± 2.00	K	NIST
Tboil	448.15 ± 2.00	K	NIST
Tboil	450.15 ± 2.00	K	NIST
Tboil	Outlier 445.90 ± 1.00	K	NIST
Tboil	Outlier 445.90 ± 1.00	K	NIST
Tboil	448.15 ± 2.00	K	NIST
Tboil	447.65 ± 3.00	K	NIST
Tboil	448.70 ± 2.00	K	NIST
Tboil	449.15 ± 2.00	K	NIST
Tboil	448.95 ± 1.00	K	NIST
Tc	[631.90; 638.50]	K
Tc	632.60	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 Compiled value
Tc	633.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	631.90	K	ChemSep v8.3 pure component data Compiled value
Tc	632.60	K	KDB
Tc	632.60 ± 0.50	K	NIST
Tc	632.00 ± 0.80	K	NIST
Tc	632.00 ± 0.60	K	NIST
Tc	632.90 ± 0.60	K	NIST
Tc	632.50	K	NIST
Tc	632.30 ± 0.15	K	NIST
Tc	633.00 ± 2.00	K	NIST
Tc	Outlier 638.50	K	NIST
Tfus	[237.15; 239.40]	K
Tfus	239.05	K	Density, Viscosity, and Freezing Point for Four Binary Systems of n-Dodecane or Methylcyclohexane Mixed with 1-Heptanol or Cyclohexylmethanol
Tfus	239.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	239.15	K	ChemSep v8.3 pure component data Compiled value
Tfus	239.00	K	KDB
Tfus	238.65	K	Aq. Solubility Prediction
Tfus	Outlier 237.15	K	NCMS SOLV-DB
Tfus	238.25 ± 0.50	K	NIST
Tfus	239.40 ± 0.50	K	NIST
Tfus	238.60 ± 0.40	K	NIST
Ttriple	[239.15; 240.00]	K
Ttriple	239.15	K	ChemSep v8.3 pure component data Compiled value
Ttriple	240.00 ± 0.20	K	NIST
Ttriple	240.00 ± 0.20	K	NIST
UQi	4.75		ChemSep v8.3 pure component data Compiled value
URi	5.27		ChemSep v8.3 pure component data Compiled value
Vc	[0.435; 0.435]	m3/kmol
Vc	0.435	m3/kmol	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 Compiled value
Vc	0.435	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.435	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.435	m3/kmol	KDB
Vc	0.435	m3/kmol	NIST
Zc	[0.2529070; 0.2610000]
Zc	0.2530000		IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 Compiled value
Zc	0.2610000		ChemSep v8.3 pure component data Compiled value
Zc	0.2529070		KDB
Zra	0.26		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[245.70; 358.80]	J/mol×K	[261.15; 380.00]
Cp,liquid	245.80	J/mol×K	261.15	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	245.70	J/mol×K	261.28	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	247.90	J/mol×K	265.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	247.90	J/mol×K	265.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	251.00	J/mol×K	270.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	250.80	J/mol×K	270.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	254.50	J/mol×K	275.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	254.30	J/mol×K	275.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	258.20	J/mol×K	280.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	258.20	J/mol×K	280.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	262.40	J/mol×K	285.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	262.40	J/mol×K	285.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	267.10	J/mol×K	290.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	267.10	J/mol×K	290.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	271.90	J/mol×K	295.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	271.70	J/mol×K	295.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	274.10	J/mol×K	298.00	NIST
Cp,liquid	278.57	J/mol×K	298.15	NIST
Cp,liquid	270.80	J/mol×K	298.15	NIST
Cp,liquid	272.29	J/mol×K	298.15	NIST
Cp,liquid	273.67	J/mol×K	298.15	NIST
Cp,liquid	276.60	J/mol×K	300.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	276.50	J/mol×K	300.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	278.90	J/mol×K	302.97	NIST
Cp,liquid	297.00	J/mol×K	303.35	NIST
Cp,liquid	281.70	J/mol×K	305.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	281.70	J/mol×K	305.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	286.80	J/mol×K	310.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	286.80	J/mol×K	310.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	292.20	J/mol×K	315.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	292.20	J/mol×K	315.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	297.50	J/mol×K	320.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	297.50	J/mol×K	320.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	303.00	J/mol×K	325.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	303.00	J/mol×K	325.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	308.50	J/mol×K	330.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	308.50	J/mol×K	330.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	313.90	J/mol×K	335.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	313.80	J/mol×K	335.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	319.10	J/mol×K	340.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	319.10	J/mol×K	340.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	324.50	J/mol×K	345.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	324.50	J/mol×K	345.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	330.30	J/mol×K	350.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	330.30	J/mol×K	350.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	335.70	J/mol×K	355.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	335.70	J/mol×K	355.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	340.60	J/mol×K	360.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	340.80	J/mol×K	360.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	345.50	J/mol×K	365.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	345.60	J/mol×K	365.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	350.20	J/mol×K	370.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	350.10	J/mol×K	370.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	354.50	J/mol×K	375.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	354.40	J/mol×K	375.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	358.80	J/mol×K	380.00	Calorimetric and FTIR study of selected aliphatic heptanols
Cp,liquid	358.70	J/mol×K	380.00	Calorimetric and FTIR study of selected aliphatic heptanols
η	[0.0015120; 0.0101470]	Pa×s	[283.15; 348.15]
η	0.0101470	Pa×s	283.15	Density and Viscosity of the Binary Systems Ethanol + Butan-1-ol, + Pentan-1-ol, + Heptan-1-ol, + Octan-1-ol, Nonan-1-ol, + Decan-1-ol at 0.1 MPa and Temperatures from 283.15 K to 313.15 K
η	0.0071040	Pa×s	293.15	Densities and Kinematic Viscosities of Ten Binary 1-Alkanol Liquid Systems at Temperatures of (293.15 and 298.15) K
η	0.0070260	Pa×s	293.15	Density and Viscosity of the Binary Systems Ethanol + Butan-1-ol, + Pentan-1-ol, + Heptan-1-ol, + Octan-1-ol, Nonan-1-ol, + Decan-1-ol at 0.1 MPa and Temperatures from 283.15 K to 313.15 K
η	0.0059140	Pa×s	298.15	Densities, Viscosities, and Volumetric Properties of Binary Mixtures of 1,2-Propanediol + 1-Heptanol or 1-Hexanol and 1,2-Ethanediol + 2-Butanol or 2-Propanol at T = (298.15, 303.15, and 308.15) K
η	0.0058510	Pa×s	298.15	Density and Viscosity of Binary Mixtures of {1-Butyl-3-methylimidazolium Thiocyanate + 1-Heptanol, 1-Octanol, 1-Nonanol, or 1-Decanol}
η	0.0059440	Pa×s	298.15	Acoustical and Excess Properties of {Chlorobenzene + 1-Hexanol, or 1-Heptanol, or 1-Octanol, or 1-Nonanol, or 1-Decanol} at (298.15, 303.15, 308.15, and 313.15) K
η	0.0059930	Pa×s	298.15	Densities and Kinematic Viscosities of Ten Binary 1-Alkanol Liquid Systems at Temperatures of (293.15 and 298.15) K
η	0.0060040	Pa×s	298.15	Densities and Viscosities of Binary Mixtures of 2,2,4-Trimethylpentane + 1-Propanol, + 1-Pentanol, + 1-Hexanol, and + 1-Heptanol from (298.15 to 323.15) K
η	0.0059470	Pa×s	298.15	Density and Viscosity of the Binary Systems Ethanol + Butan-1-ol, + Pentan-1-ol, + Heptan-1-ol, + Octan-1-ol, Nonan-1-ol, + Decan-1-ol at 0.1 MPa and Temperatures from 283.15 K to 313.15 K
η	0.0050690	Pa×s	303.15	Acoustical and Excess Properties of {Chlorobenzene + 1-Hexanol, or 1-Heptanol, or 1-Octanol, or 1-Nonanol, or 1-Decanol} at (298.15, 303.15, 308.15, and 313.15) K
η	0.0050410	Pa×s	303.15	Density and Viscosity of the Binary Systems Ethanol + Butan-1-ol, + Pentan-1-ol, + Heptan-1-ol, + Octan-1-ol, Nonan-1-ol, + Decan-1-ol at 0.1 MPa and Temperatures from 283.15 K to 313.15 K
η	0.0050451	Pa×s	303.15	Densities, Viscosities, and Volumetric Properties of Binary Mixtures of 1,2-Propanediol + 1-Heptanol or 1-Hexanol and 1,2-Ethanediol + 2-Butanol or 2-Propanol at T = (298.15, 303.15, and 308.15) K
η	0.0050790	Pa×s	303.15	Densities and Viscosities of Binary Mixtures of 2,2,4-Trimethylpentane + 1-Propanol, + 1-Pentanol, + 1-Hexanol, and + 1-Heptanol from (298.15 to 323.15) K
η	0.0050480	Pa×s	303.15	Densities, Viscosities, and Speed of Sound Studies of Binary Mixtures of Methylbenzene with Heptan-1-ol, Octan-1-ol, and Decan-1-ol at (303.15 and 313.15) K
η	0.0043403	Pa×s	308.15	Densities, Viscosities, and Volumetric Properties of Binary Mixtures of 1,2-Propanediol + 1-Heptanol or 1-Hexanol and 1,2-Ethanediol + 2-Butanol or 2-Propanol at T = (298.15, 303.15, and 308.15) K
η	0.0043330	Pa×s	308.15	Acoustical and Excess Properties of {Chlorobenzene + 1-Hexanol, or 1-Heptanol, or 1-Octanol, or 1-Nonanol, or 1-Decanol} at (298.15, 303.15, 308.15, and 313.15) K
η	0.0042600	Pa×s	308.15	Density and Viscosity of Binary Mixtures of {1-Butyl-3-methylimidazolium Thiocyanate + 1-Heptanol, 1-Octanol, 1-Nonanol, or 1-Decanol}
η	0.0043740	Pa×s	308.15	Densities and Viscosities of Binary Mixtures of 2,2,4-Trimethylpentane + 1-Propanol, + 1-Pentanol, + 1-Hexanol, and + 1-Heptanol from (298.15 to 323.15) K
η	0.0038000	Pa×s	313.15	Densities and Viscosities of Binary Mixtures of 2,2,4-Trimethylpentane + 1-Propanol, + 1-Pentanol, + 1-Hexanol, and + 1-Heptanol from (298.15 to 323.15) K
η	0.0038020	Pa×s	313.15	Density and Viscosity of the Binary Systems Ethanol + Butan-1-ol, + Pentan-1-ol, + Heptan-1-ol, + Octan-1-ol, Nonan-1-ol, + Decan-1-ol at 0.1 MPa and Temperatures from 283.15 K to 313.15 K
η	0.0037260	Pa×s	313.15	Acoustical and Excess Properties of {Chlorobenzene + 1-Hexanol, or 1-Heptanol, or 1-Octanol, or 1-Nonanol, or 1-Decanol} at (298.15, 303.15, 308.15, and 313.15) K
η	0.0037120	Pa×s	313.15	Densities, Viscosities, and Speed of Sound Studies of Binary Mixtures of Methylbenzene with Heptan-1-ol, Octan-1-ol, and Decan-1-ol at (303.15 and 313.15) K
η	0.0032240	Pa×s	318.15	Densities and Viscosities of Binary Mixtures of 2,2,4-Trimethylpentane + 1-Propanol, + 1-Pentanol, + 1-Hexanol, and + 1-Heptanol from (298.15 to 323.15) K
η	0.0031840	Pa×s	318.15	Density and Viscosity of Binary Mixtures of {1-Butyl-3-methylimidazolium Thiocyanate + 1-Heptanol, 1-Octanol, 1-Nonanol, or 1-Decanol}
η	0.0028510	Pa×s	323.15	Densities and Viscosities of Binary Mixtures of 2,2,4-Trimethylpentane + 1-Propanol, + 1-Pentanol, + 1-Hexanol, and + 1-Heptanol from (298.15 to 323.15) K
η	0.0024340	Pa×s	328.15	Density and Viscosity of Binary Mixtures of {1-Butyl-3-methylimidazolium Thiocyanate + 1-Heptanol, 1-Octanol, 1-Nonanol, or 1-Decanol}
η	0.0019000	Pa×s	338.15	Density and Viscosity of Binary Mixtures of {1-Butyl-3-methylimidazolium Thiocyanate + 1-Heptanol, 1-Octanol, 1-Nonanol, or 1-Decanol}
η	0.0015120	Pa×s	348.15	Density and Viscosity of Binary Mixtures of {1-Butyl-3-methylimidazolium Thiocyanate + 1-Heptanol, 1-Octanol, 1-Nonanol, or 1-Decanol}
ΔfusH	[18.16; 18.35]	kJ/mol	[239.90; 240.40]
ΔfusH	18.35	kJ/mol	239.90	NIST
ΔfusH	18.16	kJ/mol	240.40	NIST
ΔfusH	18.16	kJ/mol	240.40	NIST
ΔfusH	18.18	kJ/mol	240.40	NIST
ΔfusH	18.18	kJ/mol	240.40	NIST
ΔvapH	[48.12; 65.20]	kJ/mol	[310.50; 449.10]
ΔvapH	65.20	kJ/mol	310.50	NIST
ΔvapH	62.90	kJ/mol	379.00	NIST
ΔvapH	65.20	kJ/mol	391.00	NIST
ΔvapH	62.50	kJ/mol	392.50	NIST
ΔvapH	62.60	kJ/mol	393.00	NIST
ΔvapH	48.12	kJ/mol	449.10	KDB
ν	[0.0000046; 0.0000062]	m2/s	[303.15; 313.15]
ν	0.0000062	m2/s	303.15	Densities, Viscosities, and Ultrasonic Velocity Studies of Binary Mixtures of Chloroform with Pentan-1-ol, Hexan-1-ol, and Heptan-1-ol at (303.15 and 313.15) K
ν	0.0000046	m2/s	313.15	Densities, Viscosities, and Ultrasonic Velocity Studies of Binary Mixtures of Chloroform with Pentan-1-ol, Hexan-1-ol, and Heptan-1-ol at (303.15 and 313.15) K
Pvap	[7.68e-03; 111.28]	kPa	[283.40; 452.97]
Pvap	7.68e-03	kPa	283.40	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	0.01	kPa	286.20	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	0.01	kPa	289.20	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	0.02	kPa	292.20	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	0.02	kPa	292.20	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	0.02	kPa	293.20	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	0.02	kPa	293.70	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	0.03	kPa	295.20	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	0.02	kPa	295.20	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	0.03	kPa	296.70	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	0.03	kPa	298.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	0.03	kPa	298.20	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	0.03	kPa	298.30	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	0.04	kPa	301.20	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	0.04	kPa	303.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	0.05	kPa	303.20	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	0.06	kPa	304.20	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	0.08	kPa	307.20	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	0.07	kPa	308.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	0.08	kPa	308.20	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	0.09	kPa	310.20	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	0.10	kPa	313.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	0.12	kPa	313.20	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	0.11	kPa	313.20	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	0.13	kPa	315.15	NCMS SOLV-DB
Pvap	0.15	kPa	316.20	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	0.16	kPa	318.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	0.17	kPa	318.20	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	0.19	kPa	319.20	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	0.23	kPa	323.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	0.26	kPa	323.20	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	0.34	kPa	328.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	0.48	kPa	333.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	0.68	kPa	338.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	0.95	kPa	343.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	1.31	kPa	348.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	1.79	kPa	353.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	2.40	kPa	358.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	3.19	kPa	363.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	4.20	kPa	368.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	5.45	kPa	373.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	7.00	kPa	378.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	8.32	kPa	382.30	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	8.91	kPa	383.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	11.22	kPa	388.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	11.05	kPa	388.34	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	11.05	kPa	388.36	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	14.00	kPa	393.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	13.89	kPa	393.65	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	13.89	kPa	393.67	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	16.77	kPa	398.00	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	17.32	kPa	398.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	20.25	kPa	402.68	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	21.23	kPa	403.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	24.53	kPa	407.45	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	24.54	kPa	407.46	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	25.82	kPa	408.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	29.34	kPa	412.21	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	29.35	kPa	412.22	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	31.17	kPa	413.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	34.76	kPa	416.72	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	34.76	kPa	416.78	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	37.36	kPa	418.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	40.00	kPa	419.40	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap	40.12	kPa	420.40	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap	40.69	kPa	421.20	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	44.20	kPa	423.00	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap	44.48	kPa	423.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	47.55	kPa	425.69	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	47.57	kPa	425.77	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	49.44	kPa	426.27	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap	52.64	kPa	428.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	56.78	kPa	430.35	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap	60.19	kPa	432.77	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	61.94	kPa	433.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	63.50	kPa	433.75	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap	72.49	kPa	438.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	73.40	kPa	438.22	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap	74.66	kPa	439.55	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	81.04	kPa	441.44	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap	84.40	kPa	443.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	88.14	kPa	444.34	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap	92.98	kPa	446.78	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	93.13	kPa	446.82	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	93.24	kPa	446.87	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	93.24	kPa	446.87	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	93.24	kPa	446.87	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	98.12	kPa	448.60	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	98.20	kPa	448.63	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	101.30	kPa	449.52	Vapor-liquid equilibrium data of binary mixtures of 1-hexanol, 1-heptanol, 1-nonanol and 1,3-propanediol at P = 101.3 kPa using differential scanning calorimetry (DSC)
Pvap	104.37	kPa	450.73	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	110.87	kPa	452.84	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	111.28	kPa	452.97	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
n0	[1.41760; 1.42450]		[293.10; 313.15]
n0	1.42400		293.10	Viscosity and surface tension of binary systems of N,N-dimethylformamide with alkan-1-ols at different temperatures
n0	1.42397		293.15	Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrabromoethane and 1-alkanols binary mixtures
n0	1.42397		293.15	Excess molar volumes and viscosities of (1,1,2,2-tetrabromoethane + 1-alkanols) at T = (293.15 and 303.15) K
n0	1.42397		293.15	Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrachloroethane and 1-alkanols binary mixtures
n0	1.42270		293.15	Isobaric Vapor Liquid Equilibrium Data of 2-Methyl-propan-2-ol (1) + Heptan-1-ol (2), Methanol (1) + Heptan-1-ol (2), Ethanol (1) + Heptan-1-ol (2), and Propan-1-ol (1) + Heptan-1-ol (2) at 96.5 kPa
n0	1.42450		293.15	Experimental study and ERAS modeling of the excess molar enthalpy of (acetonitrile + 1-heptanol or 1-octanol) mixtures at (298.15, 313.15, and 323.15) K and atmospheric pressure
n0	1.42440		293.20	Liquid-liquid equilibrium data for systems containing of formic acid, water, and primary normal alcohols at T = 298.2 K
n0	1.42384		298.15	Atmospheric densities and interfacial tensions for 1- alkanol (1-butanol to 1-octanol) + water and ether (MTBE, ETBE, DIPE, TAME and THP) + water demixed mixtures.
n0	1.42400		298.15	NCMS SOLV-DB
n0	1.42260		298.15	Comparative study of physico-chemical properties of binary mixtures of N,N-dimethylformamide with 1-alkanols at different temperatures
n0	1.42190		298.15	Effect of Pressure on the Static Relative Permittivities of Alkan-1-ols at 298.15 K
n0	1.42240		298.15	Density, Surface Tension, and Refractive Index of Octane + 1-Alkanol Mixtures at T ) 298.15 K.
n0	1.42230		298.15	Liquid-liquid equilibrium for (water + 5-hydroxymethylfurfural + 1-pentanol/1-hexanol/1-heptanol) systems at 298.15 K
n0	1.42240		298.20	Ternary equilibrium data of mixtures consisting of 2-butanol, water, and heavy alcohols at T = 298.2 K
n0	1.42047		303.15	Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrachloroethane and 1-alkanols binary mixtures
n0	1.42040		303.15	Comparative study of physico-chemical properties of binary mixtures of N,N-dimethylformamide with 1-alkanols at different temperatures
n0	1.42002		303.15	Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrabromoethane and 1-alkanols binary mixtures
n0	1.42010		303.15	Measurements of the Properties of Binary Mixtures of Dimethylsulphoxide (DMSO) with 1-Alkanols (C4, C6, C7) at 303.15K
n0	1.41900		308.15	Comparative study of physico-chemical properties of binary mixtures of N,N-dimethylformamide with 1-alkanols at different temperatures
n0	1.41760		313.15	Comparative study of physico-chemical properties of binary mixtures of N,N-dimethylformamide with 1-alkanols at different temperatures
ρl	[770.45; 829.27]	kg/m3	[283.15; 363.15]
ρl	829.21	kg/m3	283.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl	829.27	kg/m3	283.15	Excess molar volumes of binary mixtures of 1,3-dimethylimidazolidin-2-one with an alkan-1-ol at the temperatures 283.15 K, 298.15 K, and 313.15 K
ρl	825.76	kg/m3	288.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl	825.94	kg/m3	288.15	Thermodynamic properties of mixtures containing alkoxypropanol and n-alkanol
ρl	826.20	kg/m3	288.15	Temperature dependence of the volumetric properties of some alkoxypropanols + n-alkanol mixtures
ρl	822.00	kg/m3	293.00	KDB
ρl	822.20	kg/m3	293.15	Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl	822.29	kg/m3	293.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl	803.40	kg/m3	293.15	Isobaric Vapor Liquid Equilibrium Data of Acrylonitrile (1) + Heptan-1-ol (2), Acrylonitrile (1) + Ethanol (2), and Nitrobenzene (1) + Heptan-1-ol (2) at 96.5 kPa
ρl	822.30	kg/m3	293.15	Density and Viscosity of Binary Liquid Mixtures of Ethanol + 1-Hexanol and Ethanol + 1-Heptanol from (293.15 to 328.15) K at 0.1 MPa
ρl	822.20	kg/m3	293.15	Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl	822.28	kg/m3	293.15	Density, Viscosity, Refractive Index, and Surface Tension for Six Binary Systems of Adamantane Derivatives with 1-Heptanol and Cyclohexylmethanol
ρl	822.52	kg/m3	293.15	Thermodynamics of mixtures with strongly negative deviations from Raoult s law. XII. Densities, viscosities and refractive indices at T = (293.15 to 303.15) K for (1-heptanol, or 1-decanol + cyclohexylamine) systems. Application of the ERAS model to (1-alkanol + cyclohexylamine) mixtures
ρl	822.30	kg/m3	293.15	Speeds of Sound, Densities, Isobaric Thermal Expansion, Compressibilities, and Internal Pressures of Heptan-1-ol, Octan-1-ol, Nonan-1-ol, and Decan-1-ol at Temperatures from (293 to 318) K and Pressures up to 100 MPa
ρl	818.78	kg/m3	298.15	Excess molar volumes of binary mixtures of 1,3-dimethylimidazolidin-2-one with an alkan-1-ol at the temperatures 283.15 K, 298.15 K, and 313.15 K
ρl	818.81	kg/m3	298.15	Densities and Excess Molar Volumes of Cyclopentane (1) + 1-Alkanol (2) Systems at (298.15 and 308.15) K
ρl	818.99	kg/m3	298.15	Thermodynamics of mixtures with strongly negative deviations from Raoult s law. XII. Densities, viscosities and refractive indices at T = (293.15 to 303.15) K for (1-heptanol, or 1-decanol + cyclohexylamine) systems. Application of the ERAS model to (1-alkanol + cyclohexylamine) mixtures
ρl	818.79	kg/m3	298.15	Density, Viscosity, Refractive Index, and Surface Tension for Six Binary Systems of Adamantane Derivatives with 1-Heptanol and Cyclohexylmethanol
ρl	818.79	kg/m3	298.15	Effect of chain length of alcohol on thermodynamic properties of their binary mixtures with benzylalcohol
ρl	818.79	kg/m3	298.15	FT-IR studies on excess thermodynamic properties of binary liquid mixtures o-chlorotoluene with 1-propanol, 1-butanol, 1-pentanol, 1-hexanol and 1-heptanol at different temperatures
ρl	818.85	kg/m3	298.15	Volumetric, acoustic, and viscometric studies of molecular interactions in binary mixtures of dipropylene glycol dimethyl ether with 1-alkanols at 298.15 K
ρl	819.73	kg/m3	298.15	Densities, Viscosities, and Speeds of Sound of Binary Mixtures of Heptan-1-ol with 1,4-Dioxane at Temperatures from (298.15 to 323.15) K and Atmospheric Pressure
ρl	819.20	kg/m3	298.15	Thermodynamics of 1,3-dimethylurea in eight alcohols
ρl	818.11	kg/m3	298.15	Surface Properties of Binary Mixtures of Ethylene Glycol with a Series of Aliphatic Alcohols (1-Pentanol, 1-Hexanol, and 1-Heptanol)
ρl	818.77	kg/m3	298.15	Excess molar volumes, viscosities, and speeds of sound of the ternary mixture {1-heptanol (1) + trichloroethylene (2) + methylcyclohexane (3)} at T = 298.15 K
ρl	818.80	kg/m3	298.15	Density and Viscosity of Binary Liquid Mixtures of Ethanol + 1-Hexanol and Ethanol + 1-Heptanol from (293.15 to 328.15) K at 0.1 MPa
ρl	818.80	kg/m3	298.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl	819.20	kg/m3	298.15	Temperature dependence of the volumetric properties of some alkoxypropanols + n-alkanol mixtures
ρl	818.80	kg/m3	298.15	Speeds of Sound, Densities, Isobaric Thermal Expansion, Compressibilities, and Internal Pressures of Heptan-1-ol, Octan-1-ol, Nonan-1-ol, and Decan-1-ol at Temperatures from (293 to 318) K and Pressures up to 100 MPa
ρl	818.70	kg/m3	298.15	Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl	818.48	kg/m3	298.15	Studies of Viscosities and Excess Molar Volumes of the Binary Mixtures of 1-Heptanol + 1,2-Dichloroethane, + 1,1,1-Trichloroethane, + 1,1,2,2-Tetrachloroethane, + Trichloroethylene and Tetrachloroethylene at (293.15, 298.15, and 303.15) K for the Liquid Region and at Ambient Pressure
ρl	818.75	kg/m3	298.15	Density and Relative Permittivity for 1-Alkanols + Dodecane at 298.15 K
ρl	819.00	kg/m3	298.15	Viscosities and Densities of Fatty Alcohol Mixtures from 298.15 to 338.15 K: Estimation by Kay's Rule and Prediction by the UNIFAC-VISCO and GC-UNIMOD Group Contribution Methods
ρl	818.70	kg/m3	298.15	Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl	818.79	kg/m3	298.15	Thermodynamic properties of mixtures containing alkoxypropanol and n-alkanol
ρl	818.91	kg/m3	298.20	Liquid-liquid equilibrium data for ternary systems of water + lactic acid + C4-C7 alcohols at 298.2 K and atmospheric pressure
ρl	816.18	kg/m3	303.15	Densities, Viscosities, and Speeds of Sound of Binary Mixtures of Heptan-1-ol with 1,4-Dioxane at Temperatures from (298.15 to 323.15) K and Atmospheric Pressure
ρl	815.30	kg/m3	303.15	Density and Viscosity of Binary Liquid Mixtures of Ethanol + 1-Hexanol and Ethanol + 1-Heptanol from (293.15 to 328.15) K at 0.1 MPa
ρl	815.21	kg/m3	303.15	Effect of chain length of alcohol on thermodynamic properties of their binary mixtures with benzylalcohol
ρl	815.40	kg/m3	303.15	Thermodynamics of mixtures with strongly negative deviations from Raoult s law. XII. Densities, viscosities and refractive indices at T = (293.15 to 303.15) K for (1-heptanol, or 1-decanol + cyclohexylamine) systems. Application of the ERAS model to (1-alkanol + cyclohexylamine) mixtures
ρl	815.28	kg/m3	303.15	Density, Viscosity, Refractive Index, and Surface Tension for Six Binary Systems of Adamantane Derivatives with 1-Heptanol and Cyclohexylmethanol
ρl	815.20	kg/m3	303.15	Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl	815.20	kg/m3	303.15	Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl	815.21	kg/m3	303.15	FT-IR studies on excess thermodynamic properties of binary liquid mixtures o-chlorotoluene with 1-propanol, 1-butanol, 1-pentanol, 1-hexanol and 1-heptanol at different temperatures
ρl	815.30	kg/m3	303.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl	815.27	kg/m3	303.15	Speeds of Sound, Densities, Isobaric Thermal Expansion, Compressibilities, and Internal Pressures of Heptan-1-ol, Octan-1-ol, Nonan-1-ol, and Decan-1-ol at Temperatures from (293 to 318) K and Pressures up to 100 MPa
ρl	811.60	kg/m3	308.15	Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl	812.61	kg/m3	308.15	Densities, Viscosities, and Speeds of Sound of Binary Mixtures of Heptan-1-ol with 1,4-Dioxane at Temperatures from (298.15 to 323.15) K and Atmospheric Pressure
ρl	811.72	kg/m3	308.15	Speeds of Sound, Densities, Isobaric Thermal Expansion, Compressibilities, and Internal Pressures of Heptan-1-ol, Octan-1-ol, Nonan-1-ol, and Decan-1-ol at Temperatures from (293 to 318) K and Pressures up to 100 MPa
ρl	811.69	kg/m3	308.15	Effect of chain length of alcohol on thermodynamic properties of their binary mixtures with benzylalcohol
ρl	811.60	kg/m3	308.15	Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl	811.80	kg/m3	308.15	Density and Viscosity of Binary Liquid Mixtures of Ethanol + 1-Hexanol and Ethanol + 1-Heptanol from (293.15 to 328.15) K at 0.1 MPa
ρl	811.62	kg/m3	308.15	FT-IR studies on excess thermodynamic properties of binary liquid mixtures o-chlorotoluene with 1-propanol, 1-butanol, 1-pentanol, 1-hexanol and 1-heptanol at different temperatures
ρl	811.77	kg/m3	308.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl	811.74	kg/m3	308.15	Density, Viscosity, Refractive Index, and Surface Tension for Six Binary Systems of Adamantane Derivatives with 1-Heptanol and Cyclohexylmethanol
ρl	811.90	kg/m3	308.15	Viscosities and Densities of Fatty Alcohol Mixtures from 298.15 to 338.15 K: Estimation by Kay's Rule and Prediction by the UNIFAC-VISCO and GC-UNIMOD Group Contribution Methods
ρl	812.40	kg/m3	308.15	Temperature dependence of the volumetric properties of some alkoxypropanols + n-alkanol mixtures
ρl	811.73	kg/m3	308.15	Densities and Excess Molar Volumes of Cyclopentane (1) + 1-Alkanol (2) Systems at (298.15 and 308.15) K
ρl	812.38	kg/m3	308.15	Thermodynamic properties of mixtures containing alkoxypropanol and n-alkanol
ρl	808.00	kg/m3	313.15	Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl	809.01	kg/m3	313.15	Densities, Viscosities, and Speeds of Sound of Binary Mixtures of Heptan-1-ol with 1,4-Dioxane at Temperatures from (298.15 to 323.15) K and Atmospheric Pressure
ρl	808.22	kg/m3	313.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl	808.16	kg/m3	313.15	Density, Viscosity, Refractive Index, and Surface Tension for Six Binary Systems of Adamantane Derivatives with 1-Heptanol and Cyclohexylmethanol
ρl	808.00	kg/m3	313.15	Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl	808.20	kg/m3	313.15	Density and Viscosity of Binary Liquid Mixtures of Ethanol + 1-Hexanol and Ethanol + 1-Heptanol from (293.15 to 328.15) K at 0.1 MPa
ρl	808.11	kg/m3	313.15	Excess molar volumes of binary mixtures of 1,3-dimethylimidazolidin-2-one with an alkan-1-ol at the temperatures 283.15 K, 298.15 K, and 313.15 K
ρl	808.12	kg/m3	313.15	Effect of chain length of alcohol on thermodynamic properties of their binary mixtures with benzylalcohol
ρl	808.16	kg/m3	313.15	Speeds of Sound, Densities, Isobaric Thermal Expansion, Compressibilities, and Internal Pressures of Heptan-1-ol, Octan-1-ol, Nonan-1-ol, and Decan-1-ol at Temperatures from (293 to 318) K and Pressures up to 100 MPa
ρl	804.70	kg/m3	318.15	Viscosities and Densities of Fatty Alcohol Mixtures from 298.15 to 338.15 K: Estimation by Kay's Rule and Prediction by the UNIFAC-VISCO and GC-UNIMOD Group Contribution Methods
ρl	804.60	kg/m3	318.15	Density and Viscosity of Binary Liquid Mixtures of Ethanol + 1-Hexanol and Ethanol + 1-Heptanol from (293.15 to 328.15) K at 0.1 MPa
ρl	804.63	kg/m3	318.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl	804.40	kg/m3	318.15	Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl	805.38	kg/m3	318.15	Densities, Viscosities, and Speeds of Sound of Binary Mixtures of Heptan-1-ol with 1,4-Dioxane at Temperatures from (298.15 to 323.15) K and Atmospheric Pressure
ρl	804.40	kg/m3	318.15	Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl	804.56	kg/m3	318.15	Density, Viscosity, Refractive Index, and Surface Tension for Six Binary Systems of Adamantane Derivatives with 1-Heptanol and Cyclohexylmethanol
ρl	804.55	kg/m3	318.15	Speeds of Sound, Densities, Isobaric Thermal Expansion, Compressibilities, and Internal Pressures of Heptan-1-ol, Octan-1-ol, Nonan-1-ol, and Decan-1-ol at Temperatures from (293 to 318) K and Pressures up to 100 MPa
ρl	800.70	kg/m3	323.15	Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl	801.73	kg/m3	323.15	Densities, Viscosities, and Speeds of Sound of Binary Mixtures of Heptan-1-ol with 1,4-Dioxane at Temperatures from (298.15 to 323.15) K and Atmospheric Pressure
ρl	800.70	kg/m3	323.15	Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl	801.00	kg/m3	323.15	Density and Viscosity of Binary Liquid Mixtures of Ethanol + 1-Hexanol and Ethanol + 1-Heptanol from (293.15 to 328.15) K at 0.1 MPa
ρl	800.92	kg/m3	323.15	Density, Viscosity, Refractive Index, and Surface Tension for Six Binary Systems of Adamantane Derivatives with 1-Heptanol and Cyclohexylmethanol
ρl	801.01	kg/m3	323.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl	797.24	kg/m3	328.15	Density, Viscosity, Refractive Index, and Surface Tension for Six Binary Systems of Adamantane Derivatives with 1-Heptanol and Cyclohexylmethanol
ρl	797.35	kg/m3	328.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl	797.40	kg/m3	328.15	Viscosities and Densities of Fatty Alcohol Mixtures from 298.15 to 338.15 K: Estimation by Kay's Rule and Prediction by the UNIFAC-VISCO and GC-UNIMOD Group Contribution Methods
ρl	797.40	kg/m3	328.15	Density and Viscosity of Binary Liquid Mixtures of Ethanol + 1-Hexanol and Ethanol + 1-Heptanol from (293.15 to 328.15) K at 0.1 MPa
ρl	793.65	kg/m3	333.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl	793.52	kg/m3	333.15	Density, Viscosity, Refractive Index, and Surface Tension for Six Binary Systems of Adamantane Derivatives with 1-Heptanol and Cyclohexylmethanol
ρl	789.90	kg/m3	338.15	Viscosities and Densities of Fatty Alcohol Mixtures from 298.15 to 338.15 K: Estimation by Kay's Rule and Prediction by the UNIFAC-VISCO and GC-UNIMOD Group Contribution Methods
ρl	789.91	kg/m3	338.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl	786.12	kg/m3	343.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl	782.28	kg/m3	348.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl	778.40	kg/m3	353.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl	774.45	kg/m3	358.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl	770.45	kg/m3	363.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ΔfusS	[75.60; 75.60]	J/mol×K	[240.40; 240.40]
ΔfusS	75.60	J/mol×K	240.40	NIST
ΔfusS	75.60	J/mol×K	240.40	NIST
csound,fluid	[1292.00; 1361.34]	m/s	[288.15; 308.15]
csound,fluid	1361.34	m/s	288.15	Densities, excess molar volumes, speeds of sound and isothermal compressibilities for {2-(2-hexyloxyethoxy)ethanol + n-alkanol} systems at temperatures between (288.15 and 308.15) K
csound,fluid	1344.21	m/s	293.15	Densities, excess molar volumes, speeds of sound and isothermal compressibilities for {2-(2-hexyloxyethoxy)ethanol + n-alkanol} systems at temperatures between (288.15 and 308.15) K
csound,fluid	1344.05	m/s	293.15	Thermodynamics of (1-alkanol + linear monoether) systems
csound,fluid	1328.08	m/s	298.15	Micellar Properties and Related Thermodynamic Parameters of Aqueous Anionic Surfactants in the Presence of Monohydric Alcohols
csound,fluid	1327.36	m/s	298.15	Densities, excess molar volumes, speeds of sound and isothermal compressibilities for {2-(2-hexyloxyethoxy)ethanol + n-alkanol} systems at temperatures between (288.15 and 308.15) K
csound,fluid	1326.99	m/s	298.15	Densities, Speeds of Sound, and Isentropic Compressibilities for Binary Mixtures of 1,2-Ethanediol with 2-Ethyl-1-hexanol, 1-Heptanol, or Ethanol at the Temperature 298.15 K and Densities for Mixtures of 1,2-Ethanediol with 1-Nonanol at the Temperatures (293.15 and 298.15) K
csound,fluid	1326.73	m/s	298.15	Thermodynamics of (1-alkanol + linear monoether) systems
csound,fluid	1326.65	m/s	298.15	Densities, Speeds of Sound, and Isentropic Compressibilities for Binary Mixtures of 2-Ethyl-1-hexanol with 1-Pentanol, 1-Heptanol, or 1-Nonanol at the Temperature 298.15 K
csound,fluid	1330.00	m/s	298.15	Densities, Speeds of Sound, Excess Molar Volumes, and Excess Isentropic Compressibilities at T = (298.15 and 308.15) K for Methyl Methacrylate + 1-Alkanols (1-Butanol, 1-Pentanol, and 1-Heptanol) + Cyclohexane, + Benzene, + Toluene, + p-Xylene, and + Ethylbenzene
csound,fluid	1310.68	m/s	303.15	Densities, excess molar volumes, speeds of sound and isothermal compressibilities for {2-(2-hexyloxyethoxy)ethanol + n-alkanol} systems at temperatures between (288.15 and 308.15) K
csound,fluid	1311.24	m/s	303.15	Micellar Properties and Related Thermodynamic Parameters of Aqueous Anionic Surfactants in the Presence of Monohydric Alcohols
csound,fluid	1309.93	m/s	303.15	Thermodynamics of (1-alkanol + linear monoether) systems
csound,fluid	1292.00	m/s	308.15	Densities, Speeds of Sound, Excess Molar Volumes, and Excess Isentropic Compressibilities at T = (298.15 and 308.15) K for Methyl Methacrylate + 1-Alkanols (1-Butanol, 1-Pentanol, and 1-Heptanol) + Cyclohexane, + Benzene, + Toluene, + p-Xylene, and + Ethylbenzene
csound,fluid	1294.54	m/s	308.15	Micellar Properties and Related Thermodynamic Parameters of Aqueous Anionic Surfactants in the Presence of Monohydric Alcohols
csound,fluid	1293.88	m/s	308.15	Densities, excess molar volumes, speeds of sound and isothermal compressibilities for {2-(2-hexyloxyethoxy)ethanol + n-alkanol} systems at temperatures between (288.15 and 308.15) K
γ	[0.02; 0.03]	N/m	[298.15; 323.15]
γ	0.03	N/m	298.15	Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
γ	0.03	N/m	298.15	NCMS SOLV-DB
γ	0.03	N/m	303.15	Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
γ	0.03	N/m	308.15	Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
γ	0.02	N/m	313.15	Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
γ	0.02	N/m	318.15	Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
γ	0.02	N/m	323.15	Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboilr	351.70	K	2.00	NIST

Datasets

1. Isobaric coefficient of expansion, 1/K (1)
2. Mass density, kg/m3 (7)

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	0.0008
278.15	10000.00	0.0008
278.15	15000.00	0.0008
278.15	20000.00	0.0008
278.15	25000.00	0.0007
278.15	30000.00	0.0007
278.15	35000.00	0.0007
278.15	40000.00	0.0007
278.15	45000.00	0.0007
278.15	50000.00	0.0007
278.15	55000.00	0.0007
288.15	5000.00	0.0008
288.15	10000.00	0.0008
288.15	15000.00	0.0008
288.15	20000.00	0.0008
288.15	25000.00	0.0008
288.15	30000.00	0.0007
288.15	35000.00	0.0007
288.15	40000.00	0.0007
288.15	45000.00	0.0007
288.15	50000.00	0.0007
288.15	55000.00	0.0007
298.15	5000.00	0.0008
298.15	10000.00	0.0008
298.15	15000.00	0.0008
298.15	20000.00	0.0008
298.15	25000.00	0.0008
298.15	30000.00	0.0007
298.15	35000.00	0.0007
298.15	40000.00	0.0007
298.15	45000.00	0.0007
298.15	50000.00	0.0007
298.15	55000.00	0.0007
308.15	5000.00	0.0009
308.15	10000.00	0.0008
308.15	15000.00	0.0008
308.15	20000.00	0.0008
308.15	25000.00	0.0008
308.15	30000.00	0.0008
308.15	35000.00	0.0007
308.15	40000.00	0.0007
308.15	45000.00	0.0007
308.15	50000.00	0.0007
308.15	55000.00	0.0007
318.15	5000.00	0.0009
318.15	10000.00	0.0009
318.15	15000.00	0.0008
318.15	20000.00	0.0008
318.15	25000.00	0.0008
318.15	30000.00	0.0008
318.15	35000.00	0.0008
318.15	40000.00	0.0007
318.15	45000.00	0.0007
318.15	50000.00	0.0007
318.15	55000.00	0.0007
328.15	5000.00	0.0009
328.15	10000.00	0.0009
328.15	15000.00	0.0008
328.15	20000.00	0.0008
328.15	25000.00	0.0008
328.15	30000.00	0.0008
328.15	35000.00	0.0008
328.15	40000.00	0.0008
328.15	45000.00	0.0007
328.15	50000.00	0.0007
328.15	55000.00	0.0007
338.15	5000.00	0.0009
338.15	10000.00	0.0009
338.15	15000.00	0.0009
338.15	20000.00	0.0009
338.15	25000.00	0.0008
338.15	30000.00	0.0008
338.15	35000.00	0.0008
338.15	40000.00	0.0008
338.15	45000.00	0.0008
338.15	50000.00	0.0007
338.15	55000.00	0.0007
348.15	5000.00	0.0010
348.15	10000.00	0.0009
348.15	15000.00	0.0009
348.15	20000.00	0.0009
348.15	25000.00	0.0008
348.15	30000.00	0.0008
348.15	35000.00	0.0008
348.15	40000.00	0.0008
348.15	45000.00	0.0008
348.15	50000.00	0.0008
348.15	55000.00	0.0007
Reference

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	818.7
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
313.13	1001.00	808.5
313.13	2016.00	809.2
313.13	3001.00	809.9
313.13	4001.00	810.6
313.13	4999.00	811.2
313.13	6000.00	811.9
313.13	7000.00	812.6
313.13	7996.00	813.3
313.13	8998.00	813.9
313.13	10004.00	814.6
313.13	11010.00	815.2
313.13	12000.00	815.9
313.13	12997.00	816.5
313.13	14001.00	817.2
313.13	14997.00	817.8
313.13	16001.00	818.4
313.13	16995.00	819.1
313.13	17997.00	819.7
313.13	18351.00	819.9
313.13	19000.00	820.4
313.13	20005.00	821.1
313.13	20308.00	821.3
323.09	1003.00	801.4
323.09	2013.00	802.1
323.09	3005.00	802.9
323.09	4003.00	803.5
323.09	5002.00	804.3
323.09	6000.00	805.0
323.09	7000.00	805.7
323.09	8000.00	806.4
323.09	9000.00	807.1
323.09	10010.00	807.8
323.09	11005.00	808.5
323.09	12003.00	809.2
323.09	12991.00	809.9
323.09	14001.00	810.5
323.09	15009.00	811.2
323.09	16003.00	811.9
323.09	17002.00	812.5
323.09	18002.00	813.1
323.09	19005.00	813.8
323.09	20002.00	814.4
323.09	21031.00	815.0
323.09	22007.00	815.7
333.01	1031.00	794.3
333.01	2004.00	795.1
333.01	3002.00	795.8
333.01	4025.00	796.6
333.01	5006.00	797.3
333.01	5999.00	798.1
333.01	7003.00	798.8
333.01	8013.00	799.6
333.01	8998.00	800.3
333.01	10031.00	801.1
333.01	11002.00	801.8
333.01	12004.00	802.5
333.01	13003.00	803.2
333.01	14006.00	803.9
333.01	15004.00	804.6
333.01	16030.00	805.3
333.01	17006.00	805.9
333.01	18008.00	806.6
333.01	19003.00	807.3
333.01	20017.00	808.0
333.01	21003.00	808.6
333.01	21914.00	809.2
342.68	1023.00	787.3
342.68	2006.00	788.1
342.68	3015.00	788.9
342.68	4017.00	789.7
342.68	5007.00	790.5
342.68	6001.00	791.3
342.68	6998.00	792.1
342.68	8008.00	792.9
342.68	9005.00	793.6
342.68	10015.00	794.4
342.68	11016.00	795.1
342.68	12003.00	795.9
342.68	13013.00	796.6
342.68	14005.00	797.3
342.68	15002.00	798.0
342.68	16034.00	798.7
342.68	17008.00	799.4
342.68	18009.00	800.1
342.68	19004.00	800.7
342.68	20018.00	801.4
342.68	21004.00	802.0
342.68	22006.00	802.7
352.86	1020.00	779.5
352.86	2011.00	780.4
352.86	3030.00	781.3
352.86	4017.00	782.1
352.86	5005.00	782.9
352.86	6022.00	783.8
352.86	7004.00	784.6
352.86	8007.00	785.4
352.86	9007.00	786.3
352.86	10017.00	787.0
352.86	11013.00	787.9
352.86	12003.00	788.6
352.86	13015.00	789.4
352.86	14006.00	790.2
352.86	15006.00	790.9
352.86	16034.00	791.7
352.86	17018.00	792.5
352.86	18013.00	793.2
352.86	19004.00	793.9
352.86	20030.00	794.7
352.86	21006.00	795.4
352.86	22013.00	796.1
362.73	1039.00	770.9
362.73	2024.00	771.9
362.73	3016.00	772.8
362.73	4009.00	773.7
362.73	4974.00	774.5
362.73	6005.00	775.5
362.73	7006.00	776.4
362.73	8011.00	777.3
362.73	9008.00	778.1
362.73	10010.00	779.0
362.73	11013.00	779.8
362.73	12003.00	780.6
362.73	13006.00	781.5
362.73	14006.00	782.3
362.73	15014.00	783.1
362.73	16002.00	783.9
362.73	17004.00	784.7
362.73	18000.00	785.4
362.73	19000.00	786.2
362.73	20036.00	787.0
362.73	21004.00	787.7
362.73	22002.00	788.5
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
278.15	100.00	832.4
278.15	1000.00	833.0
278.15	5000.00	835.4
278.15	10000.00	838.3
278.15	15000.00	841.2
278.15	20000.00	843.9
278.15	25000.00	846.4
278.15	30000.00	849.2
278.15	35000.00	851.7
278.15	40000.00	854.2
278.15	45000.00	856.6
278.15	50000.00	859.0
278.15	55000.00	861.3
278.15	60000.00	863.4
288.15	100.00	825.5
288.15	1000.00	826.1
288.15	5000.00	828.6
288.15	10000.00	831.7
288.15	15000.00	834.7
288.15	20000.00	837.6
288.15	25000.00	840.4
288.15	30000.00	843.1
288.15	35000.00	845.7
288.15	40000.00	848.2
288.15	45000.00	850.7
288.15	50000.00	853.1
288.15	55000.00	855.5
288.15	60000.00	857.8
298.15	100.00	818.5
298.15	1000.00	819.1
298.15	5000.00	821.8
298.15	10000.00	824.9
298.15	15000.00	828.1
298.15	20000.00	831.1
298.15	25000.00	833.9
298.15	30000.00	836.7
298.15	35000.00	839.5
298.15	40000.00	842.1
298.15	45000.00	844.7
298.15	50000.00	847.2
298.15	55000.00	849.7
298.15	60000.00	852.1
308.15	100.00	811.4
308.15	1000.00	812.1
308.15	5000.00	814.7
308.15	10000.00	818.3
308.15	15000.00	821.5
308.15	20000.00	824.6
308.15	25000.00	827.6
308.15	30000.00	830.5
308.15	35000.00	833.3
308.15	40000.00	836.0
308.15	45000.00	838.7
308.15	50000.00	841.3
308.15	55000.00	843.8
308.15	60000.00	846.1
318.15	100.00	804.3
318.15	1000.00	805.0
318.15	5000.00	807.9
318.15	10000.00	811.4
318.15	15000.00	814.8
318.15	20000.00	818.1
318.15	25000.00	821.2
318.15	30000.00	824.2
318.15	35000.00	827.1
318.15	40000.00	829.9
318.15	45000.00	832.7
318.15	50000.00	835.4
318.15	55000.00	838.0
318.15	60000.00	840.4
328.15	100.00	797.1
328.15	1000.00	797.8
328.15	5000.00	800.9
328.15	10000.00	804.6
328.15	15000.00	808.1
328.15	20000.00	811.5
328.15	25000.00	814.7
328.15	30000.00	817.8
328.15	35000.00	820.8
328.15	40000.00	823.8
328.15	45000.00	826.6
328.15	50000.00	829.4
328.15	55000.00	832.1
328.15	60000.00	834.5
338.15	100.00	789.7
338.15	1000.00	790.4
338.15	5000.00	793.7
338.15	10000.00	797.5
338.15	15000.00	801.2
338.15	20000.00	804.7
338.15	25000.00	808.1
338.15	30000.00	811.4
338.15	35000.00	814.6
338.15	40000.00	817.5
338.15	45000.00	820.6
338.15	50000.00	823.4
338.15	55000.00	826.2
338.15	60000.00	828.7
348.15	100.00	782.1
348.15	1000.00	782.9
348.15	5000.00	786.3
348.15	10000.00	790.4
348.15	15000.00	794.2
348.15	20000.00	797.9
348.15	25000.00	801.4
348.15	30000.00	804.8
348.15	35000.00	808.1
348.15	40000.00	811.3
348.15	45000.00	814.3
348.15	50000.00	817.3
348.15	55000.00	820.2
348.15	60000.00	822.8
358.15	100.00	774.2
358.15	1000.00	775.1
358.15	5000.00	778.7
358.15	10000.00	783.0
358.15	15000.00	787.1
358.15	20000.00	790.9
358.15	25000.00	794.6
358.15	30000.00	798.2
358.15	35000.00	801.5
358.15	40000.00	804.9
358.15	45000.00	808.1
358.15	50000.00	811.1
358.15	55000.00	814.1
358.15	60000.00	816.9
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	818.7
298.15	1000.00	819.3
298.15	5000.00	821.9
298.15	10000.00	824.9
298.15	15000.00	828.0
298.15	20000.00	830.8
298.15	25000.00	833.5
298.15	30000.00	836.3
298.15	35000.00	838.8
298.15	40000.00	841.3
298.15	45000.00	843.8
298.15	50000.00	846.2
298.15	55000.00	848.5
298.15	60000.00	850.8
298.15	65000.00	853.0
298.15	70000.00	855.2
298.15	80000.00	859.4
298.15	90000.00	863.5
298.15	100000.00	867.3
298.15	110000.00	871.1
298.15	120000.00	874.6
298.15	130000.00	878.1
298.15	140000.00	881.5
313.15	100.00	808.0
313.15	1000.00	808.6
313.15	5000.00	811.4
313.15	10000.00	814.7
313.15	15000.00	817.9
313.15	20000.00	821.0
313.15	25000.00	823.8
313.15	30000.00	826.8
313.15	35000.00	829.5
313.15	40000.00	832.1
313.15	45000.00	834.7
313.15	50000.00	837.2
313.15	55000.00	839.7
313.15	60000.00	842.1
313.15	65000.00	844.4
313.15	70000.00	846.7
313.15	80000.00	851.1
313.15	90000.00	855.3
313.15	100000.00	859.3
313.15	110000.00	863.2
313.15	120000.00	867.0
313.15	130000.00	870.6
313.15	140000.00	874.2
333.15	100.00	793.3
333.15	1000.00	794.0
333.15	5000.00	797.1
333.15	10000.00	800.7
333.15	15000.00	804.3
333.15	20000.00	807.7
333.15	25000.00	810.8
333.15	30000.00	813.9
333.15	35000.00	816.9
333.15	40000.00	819.8
333.15	45000.00	822.4
333.15	50000.00	825.2
333.15	55000.00	827.8
333.15	60000.00	830.3
333.15	65000.00	832.9
333.15	70000.00	835.3
333.15	80000.00	839.9
333.15	90000.00	844.5
333.15	100000.00	848.7
333.15	110000.00	852.8
333.15	120000.00	856.8
333.15	130000.00	860.5
333.15	140000.00	864.3
353.15	100.00	778.1
353.15	1000.00	778.8
353.15	5000.00	782.3
353.15	10000.00	786.3
353.15	15000.00	790.2
353.15	20000.00	793.9
353.15	25000.00	797.3
353.15	30000.00	800.7
353.15	35000.00	804.0
353.15	40000.00	807.1
353.15	45000.00	810.0
353.15	50000.00	813.0
353.15	55000.00	815.8
353.15	60000.00	818.6
353.15	65000.00	821.2
353.15	70000.00	823.8
353.15	80000.00	828.7
353.15	90000.00	833.5
353.15	100000.00	837.9
353.15	110000.00	842.3
353.15	120000.00	846.4
353.15	130000.00	850.3
353.15	140000.00	854.3
373.15	1000.00	762.8
373.15	5000.00	766.6
373.15	10000.00	771.1
373.15	15000.00	775.5
373.15	20000.00	779.5
373.15	25000.00	783.4
373.15	30000.00	787.1
373.15	35000.00	790.6
373.15	40000.00	794.0
373.15	45000.00	797.2
373.15	50000.00	800.3
373.15	55000.00	803.4
373.15	60000.00	806.3
373.15	65000.00	809.2
373.15	70000.00	811.9
373.15	80000.00	817.2
373.15	90000.00	822.3
373.15	100000.00	827.0
373.15	110000.00	831.6
373.15	120000.00	835.9
373.15	130000.00	840.2
373.15	140000.00	844.1
393.15	1000.00	745.8
393.15	5000.00	750.2
393.15	10000.00	755.3
393.15	15000.00	760.1
393.15	20000.00	764.6
393.15	25000.00	768.8
393.15	30000.00	772.9
393.15	35000.00	776.8
393.15	40000.00	780.4
393.15	45000.00	783.9
393.15	50000.00	787.3
393.15	55000.00	790.7
393.15	60000.00	793.8
393.15	65000.00	796.8
393.15	70000.00	799.8
393.15	80000.00	805.5
393.15	90000.00	810.9
393.15	100000.00	815.9
393.15	110000.00	820.8
393.15	120000.00	825.3
393.15	130000.00	829.8
393.15	140000.00	834.0
373.15	100.00	761.9
393.15	100.00	744.9
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	2002.00	819.81
298.15	3999.00	821.2
298.15	6006.00	822.3
298.15	8000.00	823.7
298.15	10002.00	824.8
298.15	12997.00	826.41
298.15	15999.00	828.31
298.15	18995.00	831.3
298.15	22001.00	833.2
298.15	25000.00	835.1
323.15	2006.00	802.09
323.15	4003.00	803.5
323.15	6000.00	804.98
323.15	7993.00	806.39
323.15	10000.00	807.79
323.15	13006.00	809.85
323.15	16007.00	811.88
323.15	19004.00	813.79
323.15	22008.00	815.68
323.15	25007.00	817.57
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	2000.00	820.2
298.15	4020.00	821.4
298.15	6010.00	822.8
298.15	8000.00	824.0
298.15	10000.00	825.3
298.15	13000.00	827.1
298.15	16000.00	828.9
298.15	19000.00	830.7
298.15	22000.00	832.5
298.15	25000.00	834.2
298.15	28000.00	835.9
298.15	29990.00	836.9
303.16	2030.00	816.5
303.16	4030.00	817.9
303.16	6040.00	819.3
303.16	7980.00	820.5
303.16	9990.00	821.8
303.16	12990.00	823.6
303.16	16020.00	825.5
303.16	19020.00	827.3
303.16	22000.00	829.2
303.16	24980.00	830.9
303.16	27980.00	832.5
303.16	30010.00	833.7
313.15	2000.00	809.2
313.15	4000.00	810.6
313.15	5980.00	811.9
313.15	7980.00	813.3
313.15	9970.00	814.6
313.15	13030.00	816.5
313.15	16020.00	818.4
313.15	19000.00	820.4
313.15	22020.00	822.2
313.15	25010.00	824.0
313.15	27980.00	825.7
313.15	30010.00	826.9
323.15	1990.00	802.1
323.15	4010.00	803.4
323.15	5990.00	804.8
323.15	8010.00	806.2
323.15	10010.00	807.6
323.15	13000.00	809.7
323.15	16000.00	811.8
323.15	18990.00	813.7
323.15	22000.00	815.6
323.15	25000.00	817.4
323.15	28000.00	819.3
323.15	30000.00	820.5
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	818.7
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[133.13; 452.92]	J/mol×K	[200.00; 1500.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K
Coefficient A			1.06760e+02
Coefficient B			-5.98850e+02
Coefficient C			6.25724e+00
Coefficient D			5.41170e-05
Coefficient E			-4.10180e-08
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	133.13	J/mol×K	200.00	Calculated Property
Cp,gas	199.74	J/mol×K	344.44	Calculated Property
Cp,gas	262.62	J/mol×K	488.89	Calculated Property
Cp,gas	313.10	J/mol×K	633.33	Calculated Property
Cp,gas	352.57	J/mol×K	777.78	Calculated Property
Cp,gas	383.45	J/mol×K	922.22	Calculated Property
Cp,gas	407.69	J/mol×K	1066.67	Calculated Property
Cp,gas	426.71	J/mol×K	1211.11	Calculated Property
Cp,gas	441.53	J/mol×K	1355.56	Calculated Property
Cp,gas	452.92	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[233.43; 383.59]	J/mol×K	[239.15; 460.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K
Coefficient A			-8.57270e+01
Coefficient B			7.42020e+02
Coefficient C			-2.19206e+00
Coefficient D			2.64410e-02
Coefficient E			-2.56740e-05
Temperature range, min.			239.15
Temperature range, max.			460.00
Cp,liquid	233.43	J/mol×K	239.15	Calculated Property
Cp,liquid	247.55	J/mol×K	263.69	Calculated Property
Cp,liquid	268.71	J/mol×K	288.23	Calculated Property
Cp,liquid	293.73	J/mol×K	312.77	Calculated Property
Cp,liquid	319.90	J/mol×K	337.31	Calculated Property
Cp,liquid	344.62	J/mol×K	361.84	Calculated Property
Cp,liquid	365.43	J/mol×K	386.38	Calculated Property
Cp,liquid	380.02	J/mol×K	410.92	Calculated Property
Cp,liquid	386.51	J/mol×K	435.46	Calculated Property
Cp,liquid	383.59	J/mol×K	460.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0956866; 0.0002513]	Pa×s	[239.15; 500.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-7.88640e+01
Coefficient B			5.89670e+03
Coefficient C			9.47210e+00
Coefficient D			-3.34660e-07
Coefficient E			2.00000e+00
Temperature range, min.			239.15
Temperature range, max.			500.00
η	0.0956866	Pa×s	239.15	Calculated Property
η	0.0195791	Pa×s	268.13	Calculated Property
η	0.0060252	Pa×s	297.12	Calculated Property
η	0.0024784	Pa×s	326.10	Calculated Property
η	0.0012606	Pa×s	355.08	Calculated Property
η	0.0007516	Pa×s	384.07	Calculated Property
η	0.0005059	Pa×s	413.05	Calculated Property
η	0.0003740	Pa×s	442.03	Calculated Property
η	0.0002977	Pa×s	471.02	Calculated Property
η	0.0002513	Pa×s	500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[76.53; 17.69]	kJ/mol	[239.15; 611.89]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K
Coefficient A			1.17318e+02
Coefficient B			1.48903e+00
Coefficient C			-2.63224e+00
Coefficient D			3.54728e+00
Coefficient E			-1.89241e+00
Critical temperature, Tc (K)			6.31900e+02
Temperature range, min.			239.15
Temperature range, max.			611.89
ΔvapH	76.53	kJ/mol	239.15	Calculated Property
ΔvapH	71.07	kJ/mol	280.57	Calculated Property
ΔvapH	65.49	kJ/mol	321.98	Calculated Property
ΔvapH	59.74	kJ/mol	363.40	Calculated Property
ΔvapH	53.84	kJ/mol	404.81	Calculated Property
ΔvapH	47.82	kJ/mol	446.23	Calculated Property
ΔvapH	41.68	kJ/mol	487.64	Calculated Property
ΔvapH	35.32	kJ/mol	529.06	Calculated Property
ΔvapH	28.21	kJ/mol	570.47	Calculated Property
ΔvapH	17.69	kJ/mol	611.89	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.64]	kPa	[344.87; 473.36]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.46759e+01
Coefficient B			-3.44597e+03
Coefficient C			-1.05377e+02
Temperature range, min.			344.87
Temperature range, max.			473.36
Pvap	1.33	kPa	344.87	Calculated Property
Pvap	2.99	kPa	359.15	Calculated Property
Pvap	6.17	kPa	373.42	Calculated Property
Pvap	11.82	kPa	387.70	Calculated Property
Pvap	21.28	kPa	401.98	Calculated Property
Pvap	36.28	kPa	416.25	Calculated Property
Pvap	59.02	kPa	430.53	Calculated Property
Pvap	92.18	kPa	444.81	Calculated Property
Pvap	138.86	kPa	459.08	Calculated Property
Pvap	202.64	kPa	473.36	Calculated Property
Pvap	[1.10e-05; 3100.47]	kPa	[239.15; 631.90]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K
Coefficient A			2.44914e+02
Coefficient B			-1.76836e+04
Coefficient C			-3.34838e+01
Coefficient D			1.76260e-05
Coefficient E			2.00000e+00
Comment			Range stopped at Tc; ChemSep gives it to 632.6 K.
Temperature range, min.			239.15
Temperature range, max.			631.90
Pvap	1.10e-05	kPa	239.15	Calculated Property
Pvap	5.43e-03	kPa	282.79	Calculated Property
Pvap	0.30	kPa	326.43	Calculated Property
Pvap	4.62	kPa	370.07	Calculated Property
Pvap	31.23	kPa	413.71	Calculated Property
Pvap	125.47	kPa	457.34	Calculated Property
Pvap	359.85	kPa	500.98	Calculated Property
Pvap	830.23	kPa	544.62	Calculated Property
Pvap	1670.53	kPa	588.26	Calculated Property
Pvap	3100.47	kPa	631.90	Calculated Property
Pvap	[1.63e-05; 2969.62]	kPa	[239.15; 631.90]	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			1.98081e+02
Coefficient B			-1.56272e+04
Coefficient C			-2.63701e+01
Coefficient D			1.17680e-05
Coefficient E			0.00000e+00
Temperature range, min.			239.15
Temperature range, max.			631.90
Pvap	1.63e-05	kPa	239.15	Calculated Property
Pvap	6.16e-03	kPa	282.79	Calculated Property
Pvap	0.31	kPa	326.43	Calculated Property
Pvap	4.57	kPa	370.07	Calculated Property
Pvap	31.12	kPa	413.71	Calculated Property
Pvap	127.11	kPa	457.34	Calculated Property
Pvap	368.82	kPa	500.98	Calculated Property
Pvap	849.17	kPa	544.62	Calculated Property
Pvap	1672.47	kPa	588.26	Calculated Property
Pvap	2969.62	kPa	631.90	Calculated Property
Pvap	[0.63; 100.85]	kPa	[336.80; 449.60]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.37681e+01
Coefficient B			-2.89385e+03
Coefficient C			-1.33487e+02
Reference			Kemme and Kreps, 1969
Temperature range, min.			336.80
Temperature range, max.			449.60
Pvap	0.63	kPa	336.80	Calculated Property
Pvap	1.43	kPa	349.33	Calculated Property
Pvap	2.99	kPa	361.87	Calculated Property
Pvap	5.79	kPa	374.40	Calculated Property
Pvap	10.49	kPa	386.93	Calculated Property
Pvap	17.96	kPa	399.47	Calculated Property
Pvap	29.30	kPa	412.00	Calculated Property
Pvap	45.84	kPa	424.53	Calculated Property
Pvap	69.11	kPa	437.07	Calculated Property
Pvap	100.85	kPa	449.60	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[861.09; 320.51]	kg/m3	[239.15; 631.90]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K
Coefficient A			6.22653e+01
Coefficient B			2.48330e-01
Coefficient C			6.32610e+02
Coefficient D			2.55560e-01
Comment			Range stopped at Tc; ChemSep gives it to 632.6 K.
Temperature range, min.			239.15
Temperature range, max.			631.90
ρl	861.09	kg/m3	239.15	Calculated Property
ρl	830.22	kg/m3	282.79	Calculated Property
ρl	797.60	kg/m3	326.43	Calculated Property
ρl	762.81	kg/m3	370.07	Calculated Property
ρl	725.24	kg/m3	413.71	Calculated Property
ρl	683.92	kg/m3	457.34	Calculated Property
ρl	637.17	kg/m3	500.98	Calculated Property
ρl	581.62	kg/m3	544.62	Calculated Property
ρl	508.10	kg/m3	588.26	Calculated Property
ρl	320.51	kg/m3	631.90	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 0.00]	N/m	[239.15; 611.89]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K
Coefficient A			-4.31650e-02
Coefficient B			-1.32750e+01
Coefficient C			-2.23470e+00
Coefficient D			-1.16140e-03
Coefficient E			-3.97730e-07
Temperature range, min.			239.15
Temperature range, max.			611.89
γ	0.03	N/m	239.15	Calculated Property
γ	0.03	N/m	280.57	Calculated Property
γ	0.02	N/m	321.98	Calculated Property
γ	0.02	N/m	363.40	Calculated Property
γ	0.02	N/m	404.81	Calculated Property
γ	0.01	N/m	446.23	Calculated Property
γ	0.01	N/m	487.64	Calculated Property
γ	0.01	N/m	529.06	Calculated Property
γ	0.00	N/m	570.47	Calculated Property
γ	0.00	N/m	611.89	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.01; 0.11]	W/m×K	[239.15; 1000.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K
Coefficient A			-6.00660e-02
Coefficient B			2.88980e-01
Coefficient C			-3.43790e+03
Coefficient D			-1.68620e+06
Temperature range, min.			239.15
Temperature range, max.			1000.00
λgas	0.01	W/m×K	239.15	Calculated Property
λgas	0.01	W/m×K	323.69	Calculated Property
λgas	0.02	W/m×K	408.23	Calculated Property
λgas	0.03	W/m×K	492.77	Calculated Property
λgas	0.04	W/m×K	577.31	Calculated Property
λgas	0.05	W/m×K	661.84	Calculated Property
λgas	0.06	W/m×K	746.38	Calculated Property
λgas	0.08	W/m×K	830.92	Calculated Property
λgas	0.09	W/m×K	915.46	Calculated Property
λgas	0.11	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.17; 0.10]	W/m×K	[239.15; 573.15]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is λliquid in W/m×K, T in K
Coefficient A			9.03590e-02
Coefficient B			1.10750e+03
Coefficient C			-1.34170e+01
Coefficient D			3.71150e-02
Coefficient E			-4.55890e-05
Temperature range, min.			239.15
Temperature range, max.			573.15
λliquid	0.17	W/m×K	239.15	Calculated Property
λliquid	0.16	W/m×K	276.26	Calculated Property
λliquid	0.16	W/m×K	313.37	Calculated Property
λliquid	0.15	W/m×K	350.48	Calculated Property
λliquid	0.14	W/m×K	387.59	Calculated Property
λliquid	0.13	W/m×K	424.71	Calculated Property
λliquid	0.12	W/m×K	461.82	Calculated Property
λliquid	0.11	W/m×K	498.93	Calculated Property
λliquid	0.10	W/m×K	536.04	Calculated Property
λliquid	0.10	W/m×K	573.15	Calculated Property

Similar Compounds

Find more compounds similar to 1-Heptanol.

Mixtures

• 5-Hydroxymethylfurfural + 1-Heptanol + Water
• 1-Heptanol + Water
• 1-Heptanol + Ethane, 1,1,2,2-tetrabromo-
• 1-Heptanol + 2-IMIDAZOLIDINONE, 1,3-DIMETHYL-
• n-Butyl ether + 1-Heptanol
• 1-Heptanol + 1-(4-Chlorophenoxy)-1-(imidazol-1-yl)-3,3-dimethylbutanone
• Carbon dioxide + 1-Heptanol
• Acetonitrile + 1-Heptanol
• Formamide, N,N-dimethyl- + 1-Heptanol
• Benzene, 1-chloro-2-methyl- + 1-Heptanol
• Lactic acid + 1-Heptanol + Water
• 1-Heptanol + Triclosan
• 1-Heptanol + Cyromazine
• 1-Heptanol + Cyclohexane
• Formic acid + 1-Heptanol + Water
• 1-Heptanol + Cyclohexylamine
• 1-Heptanol + 2-Butanol + Water
• 1-Heptanol + Diethylene glycol hexyl ether
• 1-Heptanol + Cholesterol
• 1-Heptanol + Cholesterol + Cyclohexane

Find more mixtures with 1-Heptanol.

Sources

• KDB Vapor Pressure Data
• Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
• IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 ChEDL chemicals 1.5.2, from Gude, M.; Teja, A. S. Vapor-Liquid Critical Properties of Elements and Compounds. 4. Aliphatic Alkanols. J. Chem. Eng. Data 1995, 40, 1025-1036.
• PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
• ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
• Measurements of the Properties of Binary Mixtures of Dimethylsulphoxide (DMSO) with 1-Alkanols (C4, C6, C7) at 303.15K
• Thermodynamic properties of mixtures containing alkoxypropanol and n-alkanol
• High-pressure vapor liquid and vapor liquid liquid equilibria in the carbon dioxide + 1-heptanol system
• Experimental solid-liquid phase equilibria of {cholesterol + binary solvent mixture: 1-Alcohol (C4-C10) + cyclohexane}
• Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
• Liquid-liquid phase equilibrium of (piperidinium-based ionic liquid + an alcohol) binary systems and modelling with NRHB and PCP-SAFT
• Solubility of triclosan and iodopropynyl butylcarbamate in pure alkanols at several temperatures
• Liquid-liquid equilibrium data for systems containing of formic acid, water, and primary normal alcohols at T = 298.2 K
• Liquid-liquid equilibrium data for ternary systems of water + lactic acid + C4-C7 alcohols at 298.2 K and atmospheric pressure
• Unusual behavior of the isotope effect on miscibility of 1-hexyl-3-methylimidazolium bis(trifluorosulfonyl)imide with 1-alkanols
• Atmospheric densities and interfacial tensions for 1- alkanol (1-butanol to 1-octanol) + water and ether (MTBE, ETBE, DIPE, TAME and THP) + water demixed mixtures.
• Calorimetric and FTIR study of selected aliphatic heptanols
• Solubility and dissolution characteristics of capecitabine in pure lower alcohols and water with methanol mixture solvents at atmospheric pressure and different temperatures
• Thermodynamics of mixtures with strongly negative deviations from Raoult's law. XV. Permittivities and refractive indices for 1-alkanol + n-hexylamine systems at (293.15-303.15) K. Application of the Kirkwood- Frohlich model
• Solubility determination and correlation of cyromazine in sixteen pure solvents and mixing properties of solutions
• Study of molecular interactions and preferential solvation in binary mixtures of cyclohexane and (C5-C10) 1-alkanol by Kirkwood-Buff integrals
• Temperature dependence of the volumetric properties of some alkoxypropanols + n-alkanol mixtures
• Excess molar volumes and viscosities of (1,1,2,2-tetrabromoethane + 1-alkanols) at T = (293.15 and 303.15) K
• Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrachloroethane and 1-alkanols binary mixtures
• (Liquid + liquid) phase equilibria of 1-alkyl-3-methylimidazolium methylsulfate with alcohols, or ethers, or ketones
• Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrabromoethane and 1-alkanols binary mixtures
• Excess molar volumes, viscosities, and speeds of sound of the ternary mixture {1-heptanol (1) + trichloroethylene (2) + methylcyclohexane (3)} at T = 298.15 K
• Excess molar volumes of binary mixtures of 1,3-dimethylimidazolidin-2-one with an alkan-1-ol at the temperatures 283.15 K, 298.15 K, and 313.15 K
• 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
• Volumetric, acoustic, and viscometric studies of molecular interactions in binary mixtures of dipropylene glycol dimethyl ether with 1-alkanols at 298.15 K
• Densities, excess molar volumes, speeds of sound and isothermal compressibilities for {2-(2-hexyloxyethoxy)ethanol + n-alkanol} systems at temperatures between (288.15 and 308.15) K
• Experimental study and ERAS modeling of the excess molar enthalpy of (acetonitrile + 1-heptanol or 1-octanol) mixtures at (298.15, 313.15, and 323.15) K and atmospheric pressure
• Thermodynamics of (1-alkanol + linear monoether) systems
• Isobaric thermal expansivity behaviour against temperature and pressure of associating fluids
• PrhoT measurements and derived properties of liquid 1-alkanols
• Comparative study of physico-chemical properties of binary mixtures of N,N-dimethylformamide with 1-alkanols at different temperatures
• Ternary equilibrium data of mixtures consisting of 2-butanol, water, and heavy alcohols at T = 298.2 K
• Viscosity and surface tension of binary systems of N,N-dimethylformamide with alkan-1-ols at different temperatures
• Solubility of salicylic acid in pure alcohols at different temperatures
• Liquid density of biofuel mixtures: 1-Heptanol + heptane system at pressures up to 140 MPa and temperatures from 298.15 K to 393.15 K
• FT-IR studies on excess thermodynamic properties of binary liquid mixtures o-chlorotoluene with 1-propanol, 1-butanol, 1-pentanol, 1-hexanol and 1-heptanol at different temperatures
• Application of the NRTL method to correlate solubility of diosgenin
• Solubility of climbazole in various alcohols at different temperatures
• Thermodynamics of mixtures with strongly negative deviations from Raoult s law. XII. Densities, viscosities and refractive indices at T = (293.15 to 303.15) K for (1-heptanol, or 1-decanol + cyclohexylamine) systems. Application of the ERAS model to (1-alkanol + cyclohexylamine) mixtures
• Thermodynamics of mixtures with strong negative deviations from Raoult s law. XIII. Relative permittivities for (1-alkanol + cyclohexylamine) systems, and dielectric study of (1-alkanol + polar) compound (amine, amide or ether) mixtures
• Experimental density and PC-SAFT modeling of biofuel mixtures (DBE + 1-Heptanol) at temperatures from (298.15 to 393.15) K and at pressures up to 140 MPa
• Vapor-liquid equilibrium data of binary mixtures of 1-hexanol, 1-heptanol, 1-nonanol and 1,3-propanediol at P = 101.3 kPa using differential scanning calorimetry (DSC)
• Liquid-liquid equilibrium for (water + 5-hydroxymethylfurfural + 1-pentanol/1-hexanol/1-heptanol) systems at 298.15 K
• Effect of chain length of alcohol on thermodynamic properties of their binary mixtures with benzylalcohol
• Capillary Viscometer and Vibrating Tube Densimeter for Simultaneous Measurements up to 70 MPa and 423 K
• Thermodynamics of 1,3-dimethylurea in eight alcohols
• Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
• Density, Viscosity, and Freezing Point for Four Binary Systems of n-Dodecane or Methylcyclohexane Mixed with 1-Heptanol or Cyclohexylmethanol
• Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
• Thermodynamic Functions for Solubility of 1-Hydroxybenzotriazole in Sixteen Solvents at Temperatures from (278.15 to 313.15) K and Mixing Property of Mixtures
• Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
• Solubility Modeling and Solvent Effects of Allopurinol in 15 Neat Solvents
• Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
• Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
• Viscosity and Density of n-Alcohols at Temperatures between (298.15 and 323.15) K and Pressures up to 30 MPa
• Viscosities and Densities of Fatty Alcohol Mixtures from 298.15 to 338.15 K: Estimation by Kay's Rule and Prediction by the UNIFAC-VISCO and GC-UNIMOD Group Contribution Methods
• Kirkwood-Buff Integrals, Excess Volume, and Preferential Solvation in Pentanoic Acid/(C5-C10) 1-Alkanol Binary Mixtures
• Effect of Isomerism on the Liquid-Liquid Phase Behavior of Mixtures of 1-Alkyl-3-methylimidazolium Bis((trifluoromethyl)sulfonyl)amide Ionic Liquids with Heptanol
• (r, VE, T) Measurements of the Ternary Mixture (Dibutyl Ether + 1-Heptanol + Heptane) at Temperatures up to 393.15 K and Pressures up to 140 MPa and Modeling Using the Peng-Robinson and PC-SAFT Equations of State
• Solid-Liquid Equilibrium Solubility, Thermodynamic Properties, and Molecular Simulation of Phenylphosphonic Acid in 15 Pure Solvents at Different Temperatures
• Solubility Study and Mixing Property of 3,5-Dinitro-2-methylbenzoic Acid in 13 Pure Solvents from 288.15 to 333.15 K
• Thermodynamic Properties of 1-Hexyl-3-methylimidazolium Nitrate and 1-Alkanols Mixtures: PC-SAFT Model
• Density, Surface Tension, and Refractive Index of Octane + 1-Alkanol Mixtures at T ) 298.15 K.
• Heat Capacities and Derived Thermodynamic Functions of 1-Hexanol, 1-Heptanol, 1-Octanol, and 1-Decanol between 5 K and 390 K
• Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
• Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
• Solubility and Density of 2,6-Dimethylnaphthalene in C1-C7 1-Alkanols
• Density and Relative Permittivity for 1-Alkanols + Dodecane at 298.15 K
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 5. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Methyl-3-butyl-imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using Gas-Liquid Chromatography
• Studies of Viscosities and Excess Molar Volumes of the Binary Mixtures of 1-Heptanol + 1,2-Dichloroethane, + 1,1,1-Trichloroethane, + 1,1,2,2-Tetrachloroethane, + Trichloroethylene and Tetrachloroethylene at (293.15, 298.15, and 303.15) K for the Liquid Region and at Ambient Pressure
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 8. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 9. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in Trimethyl-butylammonium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography and Static Method
• Densities, Viscosities, and Ultrasonic Velocity Studies of Binary Mixtures of Chloroform with Pentan-1-ol, Hexan-1-ol, and Heptan-1-ol at (303.15 and 313.15) K
• Effect of Pressure on the Static Relative Permittivities of Alkan-1-ols at 298.15 K
• Densities, Viscosities, and Speed of Sound Studies of Binary Mixtures of Methylbenzene with Heptan-1-ol, Octan-1-ol, and Decan-1-ol at (303.15 and 313.15) K
• Acoustical and Excess Properties of {Chlorobenzene + 1-Hexanol, or 1-Heptanol, or 1-Octanol, or 1-Nonanol, or 1-Decanol} at (298.15, 303.15, 308.15, and 313.15) K
• Thermodynamics of Mixing Tetrahydropyran with 1-Alkanols and Excess Enthalpies of Homomorphy-Related Systems
• Viscosities and Interfacial Properties of I-Methyl-3-butylimidazolium Hexafluorophosphate and 1-Isobutenyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
• Speeds of Sound, Densities, Isobaric Thermal Expansion, Compressibilities, and Internal Pressures of Heptan-1-ol, Octan-1-ol, Nonan-1-ol, and Decan-1-ol at Temperatures from (293 to 318) K and Pressures up to 100 MPa
• Thermodynamic Parameters of Anionic Surfactant-Additive Systems at the Cloud Point
• Densities, Speeds of Sound, Excess Molar Volumes, and Excess Isentropic Compressibilities at T = (298.15 and 308.15) K for Methyl Methacrylate + 1-Alkanols (1-Butanol, 1-Pentanol, and 1-Heptanol) + Cyclohexane, + Benzene, + Toluene, + p-Xylene, and + Ethylbenzene
• Liquid-Liquid Phase Behavior of Solutions of 1-Hexyl-3-methylimidazolium Bis((trifluoromethyl)sulfonyl)amide (C6mimNTf2) in n-Alkyl Alcohols
• Micellar Properties and Related Thermodynamic Parameters of Aqueous Anionic Surfactants in the Presence of Monohydric Alcohols
• Liquid Liquid Phase Behavior of Solutions of 1-Butyl-3-methylimidazolium Bis((trifluoromethyl)sulfonyl)amide (C4mimNTf2) in n-Alkyl Alcohols
• Isobaric Vapor Liquid Equilibrium Data of 2-Methyl-propan-2-ol (1) + Heptan-1-ol (2), Methanol (1) + Heptan-1-ol (2), Ethanol (1) + Heptan-1-ol (2), and Propan-1-ol (1) + Heptan-1-ol (2) at 96.5 kPa
• Isobaric Vapor Liquid Equilibrium Data of Acrylonitrile (1) + Heptan-1-ol (2), Acrylonitrile (1) + Ethanol (2), and Nitrobenzene (1) + Heptan-1-ol (2) at 96.5 kPa
• Liquid Liquid Phase Behavior of Solutions of 1,3-Dimethylimidazolium- and 1-Methyl-3-propylimidazolium Bis((trifluoromethyl)sulphonyl)amide (C1,3mimNTf2) in n-Alkyl Alcohols
• Densities, Viscosities, and Speeds of Sound of Binary Mixtures of Heptan-1-ol with 1,4-Dioxane at Temperatures from (298.15 to 323.15) K and Atmospheric Pressure
• Density and Viscosity of the Binary Systems Ethanol + Butan-1-ol, + Pentan-1-ol, + Heptan-1-ol, + Octan-1-ol, Nonan-1-ol, + Decan-1-ol at 0.1 MPa and Temperatures from 283.15 K to 313.15 K
• Isobaric Vapor Liquid Equilibria of Binary Systems (Propyl Acetate + 2-Methylbutan-1-ol), (Propyl Acetate + Hexan-1-ol), and (Propyl Acetate + Heptan-1-ol) at 101.3 kPa
• Density, Viscosity, Refractive Index, and Surface Tension for Six Binary Systems of Adamantane Derivatives with 1-Heptanol and Cyclohexylmethanol
• Comparison Study on Temperature Dependence of the Interfacial Tension of n-Alkane Water and n-Alcohol Water Two Binary Systems
• Densities and Viscosities of Binary Mixtures of 2,2,4-Trimethylpentane + 1-Propanol, + 1-Pentanol, + 1-Hexanol, and + 1-Heptanol from (298.15 to 323.15) K
• Density and Viscosity of Binary Liquid Mixtures of Ethanol + 1-Hexanol and Ethanol + 1-Heptanol from (293.15 to 328.15) K at 0.1 MPa
• Deduction of Physicochemical Properties from Solubilities: 2,4-Dihydroxybenzophenone, Biotin, and Caprolactam as Examples
• Thermodynamics of Mixing Tetrahydrofuran with 1-Alkanols and Excess Enthalpies of Homomorphy-Related Systems
• Surface Properties of Binary Mixtures of Ethylene Glycol with a Series of Aliphatic Alcohols (1-Pentanol, 1-Hexanol, and 1-Heptanol)
• Densities and Kinematic Viscosities of Ten Binary 1-Alkanol Liquid Systems at Temperatures of (293.15 and 298.15) K
• Densities and Excess Molar Volumes of Cyclopentane (1) + 1-Alkanol (2) Systems at (298.15 and 308.15) K
• Densities, Speeds of Sound, and Isentropic Compressibilities for Binary Mixtures of 2-Ethyl-1-hexanol with 1-Pentanol, 1-Heptanol, or 1-Nonanol at the Temperature 298.15 K
• Densities, Viscosities, and Volumetric Properties of Binary Mixtures of 1,2-Propanediol + 1-Heptanol or 1-Hexanol and 1,2-Ethanediol + 2-Butanol or 2-Propanol at T = (298.15, 303.15, and 308.15) K
• Density and Viscosity of Binary Mixtures of {1-Butyl-3-methylimidazolium Thiocyanate + 1-Heptanol, 1-Octanol, 1-Nonanol, or 1-Decanol}
• Densities, Speeds of Sound, and Isentropic Compressibilities for Binary Mixtures of 1,2-Ethanediol with 2-Ethyl-1-hexanol, 1-Heptanol, or Ethanol at the Temperature 298.15 K and Densities for Mixtures of 1,2-Ethanediol with 1-Nonanol at the Temperatures (293.15 and 298.15) K
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• NCMS SOLV-DB
• The Yaws Handbook of Vapor Pressure

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