Chemical Properties of Undecane (CAS 1120-21-4)

InChI

InChI=1S/C11H24/c1-3-5-7-9-11-10-8-6-4-2/h3-11H2,1-2H3

InChI Key

RSJKGSCJYJTIGS-UHFFFAOYSA-N

Formula

C11H24

SMILES

CCCCCCCCCCC

Molecular Weight¹

156.31

CAS

1120-21-4

Other Names

• Hendecane
• UN 2330
• n-C11H24
• n-undecane

• ω : Acentric Factor.
• α_p : Isobaric thermal expansion coefficient (1/K).
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_subH : Enthalpy of sublimation at a given temperature (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_c : Critical density (kg/m³).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• 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).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• 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. Datasets
4. Correlations
5. Similar Compounds
6. Mixtures
7. Sources

Physical Properties

Property	Value	Unit	Source
ω	0.5350		KDB
ΔcH°liquid	[-7431.30; -7426.40]	kJ/mol
ΔcH°liquid	-7431.30 ± 2.60	kJ/mol	NIST
ΔcH°liquid	-7426.40	kJ/mol	NIST
μ	0.00	debye	KDB
ΔfG°	41.62	kJ/mol	KDB
ΔfH°gas	[-270.50; -270.30]	kJ/mol
ΔfH°gas	-270.50	kJ/mol	KDB
ΔfH°gas	-270.30 ± 1.30	kJ/mol	NIST
ΔfH°liquid	-327.20 ± 2.60	kJ/mol	NIST
ΔfusH°	24.25	kJ/mol	Joback Calculated Property
ΔvapH°	[56.30; 56.60]	kJ/mol
ΔvapH°	56.43	kJ/mol	NIST
ΔvapH°	56.40 ± 0.40	kJ/mol	NIST
ΔvapH°	56.60 ± 0.60	kJ/mol	NIST
ΔvapH°	56.60	kJ/mol	NIST
ΔvapH°	56.44 ± 0.12	kJ/mol	NIST
ΔvapH°	56.30	kJ/mol	NIST
ΔvapH°	56.43 ± 0.08	kJ/mol	NIST
ΔvapH°	56.30 ± 0.20	kJ/mol	NIST
IE	[9.45; 9.59]	eV
IE	9.56	eV	NIST
IE	9.59	eV	NIST
IE	9.56 ± 0.10	eV	NIST
IE	9.45 ± 0.15	eV	NIST
log10WS	-6.21		Relay (1.0) Calculated Property
logPoct/wat	4.537		Crippen Calculated Property
McVol	165.850	ml/mol	McGowan Calculated Property
Pc	[1948.00; 2008.00]	kPa
Pc	1980.00	kPa	KDB
Pc	2000.00 ± 100.00	kPa	NIST
Pc	1948.00 ± 20.00	kPa	NIST
Pc	1966.00	kPa	NIST
Pc	2008.00 ± 6.00	kPa	NIST
Pc	1990.00 ± 50.00	kPa	NIST
Pc	1966.00 ± 10.00	kPa	NIST
ρc	[234.46; 276.67]	kg/m3
ρc	234.46 ± 15.63	kg/m3	NIST
ρc	276.67 ± 6.25	kg/m3	NIST
Inp	[180.44; 183.23]
Inp	180.44		NIST
Inp	183.23		NIST
Inp	180.44		NIST
S°gas	583.58	J/mol×K	NIST
S°liquid	[458.15; 464.00]	J/mol×K
S°liquid	458.15	J/mol×K	NIST
S°liquid	464.00	J/mol×K	NIST
Tboil	[466.00; 470.20]	K
Tboil	469.09	K	KDB
Tboil	469.20	K	NIST
Tboil	468.95 ± 0.50	K	NIST
Tboil	468.55 ± 0.07	K	NIST
Tboil	468.53 ± 0.07	K	NIST
Tboil	467.95 ± 0.40	K	NIST
Tboil	468.71 ± 0.20	K	NIST
Tboil	468.65 ± 0.30	K	NIST
Tboil	467.95 ± 0.30	K	NIST
Tboil	468.00 ± 0.15	K	NIST
Tboil	470.20 ± 1.50	K	NIST
Tboil	Outlier 466.00 ± 1.66	K	NIST
Tboil	470.00 ± 2.00	K	NIST
Tboil	467.65 ± 2.00	K	NIST
Tboil	469.20 ± 0.30	K	NIST
Tboil	469.04 ± 0.10	K	NIST
Tboil	469.50 ± 1.00	K	NIST
Tboil	469.10 ± 0.30	K	NIST
Tboil	468.00 ± 3.00	K	NIST
Tboil	468.70 ± 1.50	K	NIST
Tboil	468.70 ± 2.00	K	NIST
Tboil	467.70 ± 2.00	K	NIST
Tboil	469.00 ± 3.00	K	NIST
Tboil	469.20 ± 2.00	K	NIST
Tboil	468.00 ± 3.00	K	NIST
Tboil	467.60 ± 1.00	K	NIST
Tboil	470.00 ± 5.00	K	NIST
Tboil	468.99 ± 0.15	K	NIST
Tboil	467.70 ± 2.00	K	NIST
Tboil	467.70 ± 2.00	K	NIST
Tboil	468.00 ± 4.00	K	NIST
Tboil	467.00 ± 4.00	K	NIST
Tboil	467.00 ± 4.00	K	NIST
Tboil	467.00 ± 4.00	K	NIST
Tboil	467.00 ± 5.00	K	NIST
Tboil	470.00 ± 5.00	K	NIST
Tboil	470.00 ± 5.00	K	NIST
Tboil	469.00 ± 5.00	K	NIST
Tboil	470.00 ± 5.00	K	NIST
Tboil	467.70 ± 5.00	K	NIST
Tc	[637.10; 639.00]	K
Tc	639.00	K	KDB
Tc	639.00 ± 1.00	K	NIST
Tc	639.00 ± 0.30	K	NIST
Tc	638.40 ± 0.60	K	NIST
Tc	639.00 ± 0.40	K	NIST
Tc	638.80	K	NIST
Tc	638.89 ± 0.15	K	NIST
Tc	Outlier 637.10 ± 0.60	K	NIST
Tc	638.70 ± 1.00	K	NIST
Tc	638.70 ± 0.40	K	NIST
Tc	638.70 ± 0.40	K	NIST
Tc	638.73 ± 0.15	K	NIST
Tfus	[246.70; 273.15]	K
Tfus	247.50	K	KDB
Tfus	247.54 ± 0.10	K	NIST
Tfus	260.00 ± 1.66	K	NIST
Tfus	247.52 ± 0.33	K	NIST
Tfus	247.55 ± 0.02	K	NIST
Tfus	247.55 ± 0.02	K	NIST
Tfus	247.56 ± 0.01	K	NIST
Tfus	247.55 ± 0.04	K	NIST
Tfus	247.54 ± 0.06	K	NIST
Tfus	247.55 ± 0.15	K	NIST
Tfus	246.79 ± 0.20	K	NIST
Tfus	246.79 ± 0.30	K	NIST
Tfus	247.47 ± 0.10	K	NIST
Tfus	247.25 ± 0.60	K	NIST
Tfus	246.90 ± 2.00	K	NIST
Tfus	246.85 ± 0.50	K	NIST
Tfus	247.55 ± 0.50	K	NIST
Tfus	248.40 ± 0.50	K	NIST
Tfus	248.35 ± 1.00	K	NIST
Tfus	248.15 ± 2.00	K	NIST
Tfus	Outlier 273.15 ± 2.00	K	NIST
Tfus	247.54 ± 0.07	K	NIST
Tfus	247.54 ± 0.10	K	NIST
Tfus	247.25 ± 0.20	K	NIST
Tfus	247.30 ± 1.00	K	NIST
Tfus	247.50 ± 0.08	K	NIST
Tfus	247.50 ± 0.10	K	NIST
Tfus	Outlier 273.15 ± 5.00	K	NIST
Tfus	246.70 ± 1.50	K	NIST
Ttriple	[247.20; 247.59]	K
Ttriple	247.58 ± 0.05	K	NIST
Ttriple	247.59 ± 0.03	K	NIST
Ttriple	247.58 ± 0.20	K	NIST
Ttriple	247.59 ± 0.20	K	NIST
Ttriple	247.20 ± 0.30	K	NIST
Ttriple	247.59 ± 0.03	K	NIST
Ttriple	247.20 ± 0.30	K	NIST
Vc	[0.689; 0.689]	m3/kmol
Vc	0.689	m3/kmol	KDB
Vc	0.689	m3/kmol	NIST
Zc	0.2567720		KDB
Zra	0.25		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[329.70; 422.20]	J/mol×K	[250.00; 430.00]
Cp,liquid	329.70	J/mol×K	250.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	331.00	J/mol×K	260.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	333.50	J/mol×K	270.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	334.50	J/mol×K	273.15	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	336.90	J/mol×K	280.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	337.29	J/mol×K	283.15	Excess isobaric molar heat capacities and excess molar volumes for ethanol + n-decane and n-undecane systems
Cp,liquid	339.47	J/mol×K	288.15	Excess isobaric molar heat capacities and excess molar volumes for ethanol + n-decane and n-undecane systems
Cp,liquid	341.20	J/mol×K	290.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	341.10	J/mol×K	292.29	NIST
Cp,liquid	341.60	J/mol×K	293.15	Excess isobaric molar heat capacities and excess molar volumes for ethanol + n-decane and n-undecane systems
Cp,liquid	342.70	J/mol×K	298.00	NIST
Cp,liquid	345.05	J/mol×K	298.15	NIST
Cp,liquid	343.98	J/mol×K	298.15	Excess isobaric molar heat capacities and excess molar volumes for ethanol + n-decane and n-undecane systems
Cp,liquid	345.00	J/mol×K	298.15	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	345.90	J/mol×K	300.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	346.30	J/mol×K	303.15	Excess isobaric molar heat capacities and excess molar volumes for ethanol + n-decane and n-undecane systems
Cp,liquid	350.90	J/mol×K	310.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	356.20	J/mol×K	320.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	361.70	J/mol×K	330.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	367.40	J/mol×K	340.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	373.20	J/mol×K	350.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	379.20	J/mol×K	360.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	385.30	J/mol×K	370.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	391.50	J/mol×K	380.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	397.60	J/mol×K	390.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	403.80	J/mol×K	400.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	410.00	J/mol×K	410.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	416.10	J/mol×K	420.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	422.20	J/mol×K	430.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
η	[0.0008780; 0.0011990]	Pa×s	[293.15; 313.15]
η	0.0011990	Pa×s	293.15	Densities and Viscosities of Binary Mixtures of exo-Tetrahydrodicyclopentadiene with N-Undecane or N-Tetradecane at T = (293.15 to 313.15) K
η	0.0010990	Pa×s	298.15	Densities and Viscosities of Binary Mixtures of exo-Tetrahydrodicyclopentadiene with N-Undecane or N-Tetradecane at T = (293.15 to 313.15) K
η	0.0010220	Pa×s	303.15	Densities and Viscosities of Binary Mixtures of exo-Tetrahydrodicyclopentadiene with N-Undecane or N-Tetradecane at T = (293.15 to 313.15) K
η	0.0008780	Pa×s	313.15	Densities and Viscosities of Binary Mixtures of exo-Tetrahydrodicyclopentadiene with N-Undecane or N-Tetradecane at T = (293.15 to 313.15) K
ΔfusH	[6.86; 22.50]	kJ/mol	[236.60; 247.60]
ΔfusH	6.86	kJ/mol	236.60	NIST
ΔfusH	22.50	kJ/mol	247.60	NIST
ΔfusH	22.18	kJ/mol	247.60	NIST
ΔfusH	22.18	kJ/mol	247.60	NIST
ΔsubH	91.50	kJ/mol	236.00	NIST
ΔvapH	[41.51; 60.00]	kJ/mol	[299.00; 468.70]
ΔvapH	56.20	kJ/mol	299.00	NIST
ΔvapH	55.40	kJ/mol	314.00	NIST
ΔvapH	54.50	kJ/mol	324.00	NIST
ΔvapH	54.00	kJ/mol	334.00	NIST
ΔvapH	53.10	kJ/mol	344.00	NIST
ΔvapH	60.00	kJ/mol	374.00	NIST
ΔvapH	49.10	kJ/mol	424.00	NIST
ΔvapH	41.51	kJ/mol	468.70	KDB
Pvap	[40.00; 78.59]	kPa	[434.50; 458.59]
Pvap	40.00	kPa	434.50	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap	40.04	kPa	434.60	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap	45.18	kPa	438.71	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap	50.04	kPa	442.20	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap	54.82	kPa	445.40	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap	60.13	kPa	448.68	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap	65.09	kPa	451.59	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap	70.48	kPa	454.55	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap	78.59	kPa	458.59	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
n0	[1.40630; 1.41640]		[293.15; 318.15]
n0	1.41640		293.15	Activity Coefficients at Infinite Dilution and Excess Molar Volumes in Binary Mixtures Containing Normal Alkanes (Nonane, Decane, Undecane, or Dodecane) and Cresols (2-Methylphenol or 3-Methylphenol)
n0	1.40630		318.15	Thermodynamic properties of (an ester + an alkane). XVI. Experimental HEm and V Em values and a new correlation method for (an alkyl ethanoate + an n-alkane) at 318.15 K
ρl	[688.18; 747.78]	kg/m3	[283.15; 363.15]
ρl	747.78	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	747.78	kg/m3	283.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl	744.06	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	744.06	kg/m3	288.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl	740.00	kg/m3	293.00	KDB
ρl	740.35	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	739.96	kg/m3	293.15	An Isothermal vapour-liquid equilibrium data for the binary systems of CHF3 with (n-nonane, n-decane, or n-undecane) and C2F6 with (n-nonane or n-decane)
ρl	740.11	kg/m3	293.15	Activity Coefficients at Infinite Dilution of Cylcohexylamine + Octane, Toluene, Ethylbenzene, or Aniline and Excess Molar Volumes in Binary Mixtures of Cyclohexylamine + Heptane, Octane, Nonane, Decane, Undecane, Aniline, or Water
ρl	740.28	kg/m3	293.15	Excess Molar Volume along with Viscosity, Flash Point, and Refractive Index for Binary Mixtures of cis-Decalin or trans-Decalin with C9 to C11 n-Alkanes
ρl	740.35	kg/m3	293.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl	737.96	kg/m3	295.15	An Isothermal vapour-liquid equilibrium data for the binary systems of CHF3 with (n-nonane, n-decane, or n-undecane) and C2F6 with (n-nonane or n-decane)
ρl	736.48	kg/m3	297.15	An Isothermal vapour-liquid equilibrium data for the binary systems of CHF3 with (n-nonane, n-decane, or n-undecane) and C2F6 with (n-nonane or n-decane)
ρl	736.64	kg/m3	298.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl	736.64	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	740.29	kg/m3	298.15	Liquid liquid equilibrium of ternary systems 1-butyl-3-methylimidazolium hexafluorophosphate + aromatic + aliphatic
ρl	736.72	kg/m3	298.15	Liquid-liquid equilibria for (2-hydroxy benzaldehyde + n-alkane) mixtures. Intermolecular and proximity effects in systems containing hydroxyl and aldehyde groups
ρl	736.71	kg/m3	298.15	Thermodynamics of Mixtures Containing Amines. XV. Liquid Liquid Equilibria for Benzylamine + CH3(CH2)nCH3 (n = 8, 9, 10, 12, 14)
ρl	736.73	kg/m3	298.15	Liquid-liquid equilibria for aqueous sulfuric acid solutions with undecane, dodecane, or 1-dodecanol, trioctylamine or tributyl phosphate and excess and deviation properties for sub-binary systems at 298.15 K
ρl	736.63	kg/m3	298.15	Excess Molar Volume along with Viscosity, Flash Point, and Refractive Index for Binary Mixtures of cis-Decalin or trans-Decalin with C9 to C11 n-Alkanes
ρl	736.85	kg/m3	298.15	Isobaric vapor-liquid equilibrium for n-undecane + p-, o-, m-xylene at 10 kPa
ρl	735.73	kg/m3	298.15	An Isothermal vapour-liquid equilibrium data for the binary systems of CHF3 with (n-nonane, n-decane, or n-undecane) and C2F6 with (n-nonane or n-decane)
ρl	736.79	kg/m3	298.20	Apparent and Partial Molar Volumes at Infinite Dilution and Solid Liquid Equilibria of Dibenzothiophene + Alkane Systems
ρl	734.56	kg/m3	299.75	An Isothermal vapour-liquid equilibrium data for the binary systems of CHF3 with (n-nonane, n-decane, or n-undecane) and C2F6 with (n-nonane or n-decane)
ρl	732.93	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	732.93	kg/m3	303.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl	732.93	kg/m3	303.15	Excess Molar Volume along with Viscosity, Flash Point, and Refractive Index for Binary Mixtures of cis-Decalin or trans-Decalin with C9 to C11 n-Alkanes
ρl	729.23	kg/m3	308.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl	729.23	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	729.22	kg/m3	308.15	Excess Molar Volume along with Viscosity, Flash Point, and Refractive Index for Binary Mixtures of cis-Decalin or trans-Decalin with C9 to C11 n-Alkanes
ρl	725.51	kg/m3	313.15	Excess Molar Volume along with Viscosity, Flash Point, and Refractive Index for Binary Mixtures of cis-Decalin or trans-Decalin with C9 to C11 n-Alkanes
ρl	725.53	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	725.53	kg/m3	313.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl	725.69	kg/m3	313.20	Apparent and Partial Molar Volumes at Infinite Dilution and Solid Liquid Equilibria of Dibenzothiophene + Alkane Systems
ρl	721.78	kg/m3	318.15	Excess Molar Volume along with Viscosity, Flash Point, and Refractive Index for Binary Mixtures of cis-Decalin or trans-Decalin with C9 to C11 n-Alkanes
ρl	721.82	kg/m3	318.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl	721.82	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	721.82	kg/m3	318.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl	718.04	kg/m3	323.15	Excess Molar Volume along with Viscosity, Flash Point, and Refractive Index for Binary Mixtures of cis-Decalin or trans-Decalin with C9 to C11 n-Alkanes
ρl	718.11	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	718.11	kg/m3	323.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl	714.39	kg/m3	328.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl	714.39	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	710.68	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	710.68	kg/m3	333.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl	706.95	kg/m3	338.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl	706.95	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	703.22	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	703.22	kg/m3	343.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl	699.47	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	699.47	kg/m3	348.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl	695.72	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	695.72	kg/m3	353.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl	691.96	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	691.96	kg/m3	358.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl	688.18	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
ρl	688.18	kg/m3	363.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ΔfusS	29.00	J/mol×K	236.60	NIST
γ	0.02	N/m	293.20	KDB

Datasets

1. Isobaric coefficient of expansion, 1/K (1)
2. Mass density, kg/m3 (4)

Isobaric coefficient of expansion, 1/K

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

Mass density, kg/m3

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
1000.00	278.00	752.64
20000.00	278.00	764.19
40000.00	278.00	775.36
60000.00	278.00	785.14
1000.00	288.00	745.18
20000.00	288.00	757.29
40000.00	288.00	768.82
60000.00	288.00	778.9
1000.00	298.00	737.58
20000.00	298.00	750.5
40000.00	298.00	762.53
60000.00	298.00	773.01
1000.00	308.00	729.86
20000.00	308.00	743.8
40000.00	308.00	756.47
60000.00	308.00	767.47
1000.00	318.00	722.02
20000.00	318.00	737.19
40000.00	318.00	750.63
60000.00	318.00	762.26
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
313.24	8029.00	733.14
313.18	9997.00	734.69
313.19	12016.00	736.18
313.22	14009.00	737.62
313.23	16006.00	739.05
313.19	18013.00	740.5
313.17	19009.00	741.21
323.24	7997.00	726.03
323.22	10009.00	727.67
323.23	12003.00	729.24
323.23	14022.00	730.8
323.19	16026.00	732.35
323.19	17995.00	733.8
323.18	19002.00	734.54
333.14	8001.00	718.68
333.16	10001.00	720.38
333.13	12007.00	722.07
333.15	14012.00	723.7
333.12	16003.00	725.32
333.12	17990.00	726.87
333.14	19027.00	727.66
343.29	7989.00	711.51
343.29	9998.00	713.33
343.26	11021.00	714.27
343.28	11999.00	715.12
343.25	13005.00	716.0
343.26	14019.00	716.86
343.30	14998.00	717.66
343.27	15997.00	718.51
343.25	16996.00	719.36
343.27	18006.00	720.27
343.28	19019.00	720.98
353.33	7993.00	704.36
353.35	9996.00	706.27
353.31	11002.00	707.25
353.16	12003.00	708.19
353.32	13007.00	709.08
353.33	14003.00	709.98
353.32	14999.00	710.86
353.34	16001.00	711.73
353.31	17012.00	712.63
353.33	18010.00	713.48
353.32	19024.00	714.35
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
313.15	1000.00	726.6
313.15	2001.00	727.3
313.15	3001.00	728.0
313.15	4000.00	728.7
313.15	5000.00	729.5
313.15	6001.00	730.2
313.15	7000.00	731.0
313.15	8000.00	731.8
313.15	9000.00	732.6
313.15	10000.00	733.4
313.15	11000.00	734.1
313.15	12000.00	734.9
313.15	13000.00	735.7
313.15	14001.00	736.4
313.15	15000.00	737.2
313.15	16000.00	737.9
313.15	17000.00	738.7
313.15	18000.00	739.4
313.15	19000.00	740.0
313.15	20000.00	740.7
313.15	21001.00	741.3
313.15	22000.00	742.0
313.15	23000.00	742.6
313.15	24000.00	743.2
313.15	25000.00	743.7
323.10	1000.00	719.0
323.10	2000.00	719.8
323.10	3000.00	720.6
323.10	4000.00	721.4
323.10	5001.00	722.2
323.10	6000.00	723.0
323.10	7000.00	723.8
323.10	8000.00	724.6
323.10	9000.00	725.5
323.10	10001.00	726.3
323.10	11000.00	727.1
323.10	12000.00	727.9
323.10	13000.00	728.7
323.10	14000.00	729.5
323.10	15001.00	730.3
323.10	16000.00	731.1
323.10	17000.00	731.9
323.10	18000.00	732.6
323.10	19000.00	733.3
323.10	20000.00	734.0
323.10	21000.00	734.7
323.10	22000.00	735.4
323.10	23000.00	736.0
323.10	24000.00	736.7
323.10	25000.00	737.3
333.02	1000.00	711.3
333.02	2001.00	712.1
333.02	3000.00	713.0
333.02	4000.00	713.8
333.02	5000.00	714.7
333.02	6000.00	715.5
333.02	7000.00	716.4
333.02	8001.00	717.3
333.02	9000.00	718.1
333.02	10000.00	719.0
333.02	11000.00	719.9
333.02	12000.00	720.7
333.02	13000.00	721.5
333.02	14000.00	722.4
333.02	15000.00	723.2
333.02	16000.00	724.0
333.02	17000.00	724.8
333.02	18000.00	725.6
333.02	19000.00	726.3
333.02	20000.00	727.1
333.02	21000.00	727.8
333.02	22000.00	728.5
333.02	23000.00	729.2
333.02	24000.00	729.9
333.02	25000.00	730.5
342.09	1000.00	703.9
342.09	2000.00	704.8
342.09	3001.00	705.8
342.09	4000.00	706.7
342.09	5000.00	707.6
342.09	6000.00	708.5
342.09	7000.00	709.4
342.09	8000.00	710.4
342.09	9000.00	711.2
342.09	10000.00	712.2
342.09	11000.00	713.1
342.09	12000.00	714.0
342.09	13000.00	714.8
342.09	14000.00	715.7
342.09	15000.00	716.6
342.09	16000.00	717.4
342.09	17000.00	718.2
342.09	18000.00	719.1
342.09	19000.00	719.9
342.09	20000.00	720.6
342.09	21000.00	721.4
342.09	22000.00	722.2
342.09	23000.00	722.9
342.09	23999.00	723.6
342.09	25000.00	724.3
352.93	1000.00	696.5
352.93	2000.00	697.4
352.93	3001.00	698.4
352.93	4000.00	699.4
352.93	5000.00	700.4
352.93	6000.00	701.4
352.93	7001.00	702.3
352.93	8000.00	703.3
352.93	9000.00	704.3
352.93	10001.00	705.2
352.93	11000.00	706.2
352.93	12000.00	707.1
352.93	13000.00	708.0
352.93	14000.00	709.0
352.93	15000.00	709.8
352.93	16000.00	710.7
352.93	17000.00	711.6
352.93	18000.00	712.5
352.93	19000.00	713.3
352.93	20000.00	714.1
352.93	21000.00	715.0
352.93	22000.00	715.7
352.93	23000.00	716.5
352.93	24000.00	717.3
352.93	25000.00	718.0
362.91	1000.00	688.8
362.91	2001.00	689.9
362.91	3000.00	691.0
362.91	4000.00	692.0
362.91	5001.00	693.1
362.91	6001.00	694.1
362.91	7001.00	695.2
362.91	8000.00	696.2
362.91	9000.00	697.2
362.91	10000.00	698.2
362.91	11000.00	699.2
362.91	12001.00	700.2
362.91	13000.00	701.1
362.91	14001.00	702.1
362.91	15001.00	703.0
362.91	16001.00	704.0
362.91	17001.00	704.9
362.91	18000.00	705.8
362.91	19001.00	706.6
362.91	20000.00	707.5
362.91	21000.00	708.4
362.91	22000.00	709.2
362.91	23000.00	710.0
362.91	24000.00	710.9
362.91	25000.00	711.6
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
100.00	283.15	747.8
100.00	288.15	744.1
100.00	293.15	740.5
100.00	298.15	736.5
100.00	303.15	732.9
100.00	308.15	729.2
100.00	313.15	725.5
100.00	318.15	721.9
100.00	323.15	718.1
10000.00	283.15	754.2
10000.00	288.15	750.7
10000.00	293.15	747.2
10000.00	298.15	743.6
10000.00	303.15	740.1
10000.00	308.15	736.7
10000.00	313.15	733.1
10000.00	318.15	729.6
10000.00	323.15	726.0
20000.00	283.15	760.4
20000.00	288.15	757.0
20000.00	293.15	753.6
20000.00	298.15	750.2
20000.00	303.15	746.8
20000.00	308.15	743.5
20000.00	313.15	740.2
20000.00	318.15	736.9
20000.00	323.15	733.5
30000.00	283.15	766.1
30000.00	288.15	762.9
30000.00	293.15	759.6
30000.00	298.15	756.4
30000.00	303.15	753.1
30000.00	308.15	749.9
30000.00	313.15	746.8
30000.00	318.15	743.5
30000.00	323.15	740.3
40000.00	283.15	771.5
40000.00	288.15	768.4
40000.00	293.15	765.3
40000.00	298.15	762.0
40000.00	303.15	758.9
40000.00	308.15	755.9
40000.00	313.15	752.9
40000.00	318.15	749.7
40000.00	323.15	746.7
50000.00	283.15	776.6
50000.00	288.15	773.5
50000.00	293.15	770.6
50000.00	298.15	767.5
50000.00	303.15	764.4
50000.00	308.15	761.4
50000.00	313.15	758.5
50000.00	318.15	755.5
50000.00	323.15	752.5
60000.00	283.15	781.4
60000.00	288.15	778.5
60000.00	293.15	775.6
60000.00	298.15	772.6
60000.00	303.15	769.7
60000.00	308.15	766.7
60000.00	313.15	763.9
60000.00	318.15	761.0
60000.00	323.15	758.0
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[238.83; 586.83]	J/mol×K	[273.00; 1000.00]	Joback Predicted correlation
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K
Coefficient A			-7.11100e+00
Coefficient B			1.04884e+00
Coefficient C			-5.74600e-04
Coefficient D			1.19700e-07
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	238.83	J/mol×K	273.00	Calculated Property
Cp,gas	297.33	J/mol×K	353.78	Calculated Property
Cp,gas	349.98	J/mol×K	434.56	Calculated Property
Cp,gas	397.18	J/mol×K	515.33	Calculated Property
Cp,gas	439.29	J/mol×K	596.11	Calculated Property
Cp,gas	476.69	J/mol×K	676.89	Calculated Property
Cp,gas	509.77	J/mol×K	757.67	Calculated Property
Cp,gas	538.90	J/mol×K	838.44	Calculated Property
Cp,gas	564.46	J/mol×K	919.22	Calculated Property
Cp,gas	586.83	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.63]	kPa	[348.32; 498.95]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.45189e+01
Coefficient B			-3.92882e+03
Coefficient C			-7.22530e+01
Temperature range, min.			348.32
Temperature range, max.			498.95
Pvap	1.33	kPa	348.32	Calculated Property
Pvap	3.01	kPa	365.06	Calculated Property
Pvap	6.21	kPa	381.79	Calculated Property
Pvap	11.91	kPa	398.53	Calculated Property
Pvap	21.44	kPa	415.27	Calculated Property
Pvap	36.52	kPa	432.00	Calculated Property
Pvap	59.35	kPa	448.74	Calculated Property
Pvap	92.54	kPa	465.48	Calculated Property
Pvap	139.14	kPa	482.21	Calculated Property
Pvap	202.63	kPa	498.95	Calculated Property
Pvap	[3.78e-04; 1980.25]	kPa	[247.57; 638.76]	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			1.34087e+02
Coefficient B			-1.15852e+04
Coefficient C			-1.73722e+01
Coefficient D			9.45325e-06
Coefficient E			0.00000e+00
Temperature range, min.			247.57
Temperature range, max.			638.76
Pvap	3.78e-04	kPa	247.57	Calculated Property
Pvap	0.03	kPa	291.04	Calculated Property
Pvap	0.63	kPa	334.50	Calculated Property
Pvap	5.40	kPa	377.97	Calculated Property
Pvap	26.69	kPa	421.43	Calculated Property
Pvap	91.24	kPa	464.90	Calculated Property
Pvap	242.59	kPa	508.36	Calculated Property
Pvap	542.83	kPa	551.83	Calculated Property
Pvap	1079.12	kPa	595.29	Calculated Property
Pvap	1980.25	kPa	638.76	Calculated Property
Pvap	[5.31; 104.80]	kPa	[377.61; 470.42]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.40495e+01
Coefficient B			-3.62076e+03
Coefficient C			-8.51280e+01
Reference			Camin and Rossini, 1955
Temperature range, min.			377.61
Temperature range, max.			470.42
Pvap	5.31	kPa	377.61	Calculated Property
Pvap	8.10	kPa	387.92	Calculated Property
Pvap	12.01	kPa	398.23	Calculated Property
Pvap	17.36	kPa	408.55	Calculated Property
Pvap	24.54	kPa	418.86	Calculated Property
Pvap	33.97	kPa	429.17	Calculated Property
Pvap	46.14	kPa	439.48	Calculated Property
Pvap	61.60	kPa	449.80	Calculated Property
Pvap	80.94	kPa	460.11	Calculated Property
Pvap	104.80	kPa	470.42	Calculated Property

Similar Compounds

Find more compounds similar to Undecane.

Mixtures

• Undecane + Carbon dioxide
• Benzene + Undecane
• Undecane + Acetic acid, methyl ester
• Undecane + Ethyl Acetate
• Undecane + Acetic acid, propyl ester
• Undecane + Acetic acid, butyl ester
• Undecane + Acetic acid, pentyl ester
• Undecane + Methyl Alcohol
• Undecane + Acetic acid, methyl ester + Methyl Alcohol
• Undecane + Carbon dioxide + Ethanol
• Undecane + Octadecane
• Undecane + Formamide, N-methyl-
• Undecane + Pyridine
• Undecane + p-Xylene
• Undecane + o-Xylene
• Undecane + Benzene, 1,3-dimethyl-
• Undecane + Acetonitrile
• Undecane + 9H-Fluoren-9-one
• Thianthrene + Undecane
• Undecane + 9H-Xanthene

Find more mixtures with Undecane.

Sources

• KDB Vapor Pressure Data
• Cheméo Relay (1.0)
• Crippen Method
• Crippen Method
• Solubility of 9-fluorenone, thianthrene and xanthene in organic solvents
• Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent
• New isothermal vapor liquid equilibria for the CO2 + n-nonane, and CO2 + n-undecane systems
• Liquid liquid equilibrium of ternary systems 1-butyl-3-methylimidazolium hexafluorophosphate + aromatic + aliphatic
• Liquid liquid equilibrium of ternary systems 1-octyl-3-methylimidazolium hexafluorophosphate + aromatic + aliphatic hydrocarbons
• Determination and correlation of liquid-liquid equilibria for nine binary acetonitrile + n-alkane systems
• Liquid-liquid equilibria for aqueous sulfuric acid solutions with undecane, dodecane, or 1-dodecanol, trioctylamine or tributyl phosphate and excess and deviation properties for sub-binary systems at 298.15 K
• Isobaric vapor-liquid equilibrium for n-undecane + p-, o-, m-xylene at 10 kPa
• Study of critical and maximum temperatures of coexistence of liquid and gas phase in hydrocarbons binary mixtures of aromatic hydrocarbons with alkanes and cycloalkanes
• Experimental and theoretical study of interaction between organic compounds and 1- (4-sulfobutyl)-3-methylimidazolium based ionic liquids
• Study of interaction between organic compounds and mono or dicationic oxygenated ionic liquids using gas chromatography
• Experimental measurements and thermodynamic modeling of wax disappearance temperature for the binary systems n-C14H30 + n- C16H34, n-C16H34 + n-C18H38 and n-C11H24 + n-C18H38
• Abraham model linear free energy relationships for describing the partitioning and solubility behavior of nonelectrolyte organic solutes dissolved in pyridine at 298.15 K
• Measurement and correlation of the interfacial tension for paraffin + CO2 and (CO2+N2) mixture gas at elevated temperatures and pressures
• An Isothermal vapour-liquid equilibrium data for the binary systems of CHF3 with (n-nonane, n-decane, or n-undecane) and C2F6 with (n-nonane or n-decane)
• CO2 and alkane minimum miscible pressure estimation by the extrapolation of interfacial tension
• Thermodynamic properties of (an ester + an alkane). XVI. Experimental HEm and V Em values and a new correlation method for (an alkyl ethanoate + an n-alkane) at 318.15 K
• Liquid--liquid equilibria for mixtures of {methyl acetate + methanol + n-alkane (C10--C12)} at several temperatures and 1 atm
• Excess isobaric molar heat capacities and excess molar volumes for ethanol + n-decane and n-undecane systems
• Thermodynamic properties of (an ester + and alkane). XVII. Experimental He and Ve values for (an alkyl propanoate + an alkane) at 318.15K
• Activity coefficients at infinite dilution of hydrocarbons, alkylbenzenes, and alcohols in the paramagnetic ionic liquid 1-butyl-3-methyl-imidazolium tetrachloridoferrate(III) using gas liquid chromatography
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-octyl-3-methylimidazolium hexafluorophosphate using gas liquid chromatography at T = (313.15, 323.15, and 333.15) K
• High pressure density and speed-of-sound measurements in n-undecane and evidence of the effects of near-field diffraction
• Thermodynamics of solvation in propylene glycol and methyl cellosolve
• Activity coefficients at infinite dilution of organic solutes in methylphosphonate based ionic liquids using gas-liquid chromatography
• Experiment and correlation of the equilibrium interfacial tension for paraffin + CO2 modified with ethanol
• Liquid-liquid equilibria for (2-hydroxy benzaldehyde + n-alkane) mixtures. Intermolecular and proximity effects in systems containing hydroxyl and aldehyde groups
• Standard molar Gibbs free energy and enthalpy of solvation of lowpolar solutes in formamide derivatives at 298 K
• Density and Volumetric Behavior of CO2 + Undecane System from 313.15 to 353.15 K and Pressures up to 19 MPa
• Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
• 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
• Interfacial Tension Measurement and Calculation of (Carbon Dioxide + n-Alkane) Binary Mixtures
• Determination of Infinite Dilution Activity Coefficients of Several Organic Solutes in N-Butylpyridinium Nitrate/N-Octylpyridinium Nitrate by Blend Inverse Gas Chromatography
• Measurement and Correlation of High Pressure Phase Equilibria for CO2 + Alkanes and CO2 + Crude Oil Systems
• Determination of Activity Coefficients at Infinite Dilution of Solutes in N,N'-Di(2-ethylhexyl)isobutyramide Using Inverse Gas-Liquid Chromatography
• Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
• Vapor-Liquid-Liquid Equilibria, Azeotropic, and Excess Enthalpy Data for the Binary System n-Undecane + Propionamide, and Pure Component Vapor Pressure and Density Data for Propionamide
• Activity Coefficients at Infinite Dilution and Excess Molar Volumes in Binary Mixtures Containing Normal Alkanes (Nonane, Decane, Undecane, or Dodecane) and Cresols (2-Methylphenol or 3-Methylphenol)
• 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
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 6. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Methyl-3-octyl-imidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Activity Coefficients at Infinite Dilution of Cylcohexylamine + Octane, Toluene, Ethylbenzene, or Aniline and Excess Molar Volumes in Binary Mixtures of Cyclohexylamine + Heptane, Octane, Nonane, Decane, Undecane, Aniline, or Water
• 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
• Determination of Partitioning Coefficients of Numerous Organic Solutes between a Long-Chain Aliphatic Alcohol and the Gas Phase as a Function of Temperature
• 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 and Viscosities of Binary Mixtures of exo-Tetrahydrodicyclopentadiene with N-Undecane or N-Tetradecane at T = (293.15 to 313.15) K
• Activity Coefficients at Infinite Dilution of Organic Compounds in Four New Imidazolium-Based Ionic Liquids
• Apparent and Partial Molar Volumes at Infinite Dilution and Solid Liquid Equilibria of Dibenzothiophene + Alkane Systems
• Liquid Liquid Equilibria of the Ternary Systems Undecane + 1,4-Diethylbenzene + Tetrahydrothiophene 1,1-Dioxide and Tridecane + 1,4-Diethylbenzene + Tetrahydrothiophene 1,1-Dioxide at T = (323.15, 348.15, and 373.15) K
• Partition Coefficients of Organic Compounds in Four New Tetraalkylammonium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Using Inverse Gas Chromatography
• Evaluation of the Performance of Trigeminal Tricationic Ionic Liquids for Separation Problems
• Activity Coefficients at Infinite Dilution for Organic Compounds Dissolved in 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Having Six-, Eight-, and Ten-Carbon Alkyl Chains
• Densities of Cresols and Linear Alkane Mixtures at High Pressure
• Activity Coefficients at Infinite Dilution for Organic Solutes Dissolved in Three 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Bearing Short Linear Alkyl Side Chains of Three to Five Carbons
• Excess Molar Volume along with Viscosity, Flash Point, and Refractive Index for Binary Mixtures of cis-Decalin or trans-Decalin with C9 to C11 n-Alkanes
• Infinite Dilution Activity Coefficients of Solutes Dissolved in Two Trihexyl(tetradecyl)phosphonium Ionic Liquids
• Thermodynamics of Mixtures Containing Amines. XV. Liquid Liquid Equilibria for Benzylamine + CH3(CH2)nCH3 (n = 8, 9, 10, 12, 14)
• Thermophysical Characterization of Liquids Using Precise Density and Isobaric Heat Capacity Measurements As a Function of Pressure
• Activity Coefficients at Infinite Dilution of Organic Compounds in Trihexyl(tetradecyl)phosphonium Bis(trifluoromethylsulfonyl)imide Using Inverse Gas Chromatography
• Paramagnetic Ionic Liquid 1-Butyl-3-methylimidazolium Tetrabromidocobaltate(II): Activity Coefficients at Infinite Dilution of Organic Solutes and Crystal Structure
• Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
• Isobaric Thermal Expansivity for Nonpolar Compounds
• Study of Ether-, Alcohol-, or Cyano-Functionalized Ionic Liquids Using Inverse Gas Chromatography
• Miscibility of Trihexyl(tetradecyl)phosphonium Chloride with Alkanes
• Joback Method
• KDB
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure
• Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD

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