Chemical Properties of Pentane (CAS 109-66-0)

InChI

InChI=1S/C5H12/c1-3-5-4-2/h3-5H2,1-2H3

InChI Key

OFBQJSOFQDEBGM-UHFFFAOYSA-N

Formula

C5H12

SMILES

CCCCC

Molecular Weight¹

72.15

CAS

109-66-0

Other Names

• Amyl hydride
• NSC 72415
• PENTYL HYDRIDE
• Pentan
• Pentanen
• Pentani
• Skellysolve A
• n-C5H12
• n-pentane

• ω : Acentric Factor.
• T_ig : Autoignition Temperature (K).
• AP : Aniline Point (K).
• Δ_cH°_gas : Standard gas enthalpy of combustion (kJ/mol).
• 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).
• ε_r : Dielectric Constant (Relative permittivity).
• LFL : Lower Flammability Limit (% in Air).
• UFL : Upper Flammability Limit (% in Air).
• T_flash,cc : Flash Point (Closed Cup Method) (K).
• T_flash,oc : Flash Point (Open Cup Method) (K).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• R_g : Radius of Gyration.
• Δ_c,grossH : Heat of Combustion, Gross form (kJ/mol).
• Δ_c,netH : Heat of Combustion, Net Form (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).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• NFPA Safety : NFPA Safety Rating.
• 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).
• 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).
• Δ_vapS : Entropy of vaporization at a given temperature (J/mol×K).
• T_boil : Normal Boiling Point Temperature (K).
• T_boil(P) : Boiling point at given pressure (K).
• T_c : Critical Temperature (K).
• λ_gas : Gas thermal conductivity (W/m×K).
• λ_liquid : Liquid thermal conductivity (W/m×K).
• α_diff : Thermal diffusivity (m²/s).
• 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).
• V_COSTALD : COSTALD Characteristic Volume (m³/kmol).
• ω_SRK : SRK acentric factor.
• 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	[0.2510; 0.2510]
ω	0.2510		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.2510		Passut and Danner (1973), critical constants and acentric factors Compiled value
ω	0.2510		ChemSep v8.3 pure component data Compiled value
ω	0.2510		KDB
Tig	[533.15; 557.59]	K
Tig	557.59	K	KDB
Tig	533.15	K	NCMS SOLV-DB
AP	343.850	K	KDB
ΔcH°gas	[-3536.60; -3535.40]	kJ/mol
ΔcH°gas	-3535.40 ± 0.96	kJ/mol	NIST
ΔcH°gas	-3536.60 ± 0.88	kJ/mol	NIST
ΔcH°liquid	[-3509.50; -3509.00]	kJ/mol
ΔcH°liquid	-3509.00 ± 0.46	kJ/mol	NIST
ΔcH°liquid	-3509.50 ± 0.59	kJ/mol	NIST
ΔcH°liquid	-3509.20 ± 0.75	kJ/mol	NIST
μ	[0.00; 0.00]	debye
μ	0.00	debye	ChemSep v8.3 pure component data Compiled value
μ	0.00	debye	KDB
εr	1.84		NCMS SOLV-DB
LFL	1.40	% in Air	KDB
UFL	8.30	% in Air	KDB
Tflash,cc	233.15	K	NCMS SOLV-DB
Tflash,oc	223.71	K	KDB
ΔfG°	[-8.81; -8.37]	kJ/mol
ΔfG°	-8.81	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	-8.37	kJ/mol	KDB
Rg	3.3850		KDB
Δc,grossH	3509.41	kJ/mol	KDB
Δc,netH	3245.361	kJ/mol	KDB
ΔfH°gas	[-147.10; -146.40]	kJ/mol
ΔfH°gas	-146.76	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-146.50	kJ/mol	KDB
ΔfH°gas	-146.80 ± 0.59	kJ/mol	NIST
ΔfH°gas	-147.10 ± 1.00	kJ/mol	NIST
ΔfH°gas	-146.40 ± 0.67	kJ/mol	NIST
ΔfH°liquid	[-173.50; -173.10]	kJ/mol
ΔfH°liquid	-173.50 ± 0.59	kJ/mol	NIST
ΔfH°liquid	-173.10 ± 0.67	kJ/mol	NIST
ΔfusH°	8.71	kJ/mol	Joback Calculated Property
ΔvapH°	[26.20; 27.40]	kJ/mol
ΔvapH°	26.44	kJ/mol	NCMS SOLV-DB
ΔvapH°	26.75	kJ/mol	NIST
ΔvapH°	26.20	kJ/mol	NIST
ΔvapH°	26.40	kJ/mol	NIST
ΔvapH°	26.60 ± 0.10	kJ/mol	NIST
ΔvapH°	26.40	kJ/mol	NIST
ΔvapH°	26.40	kJ/mol	NIST
ΔvapH°	26.70 ± 0.40	kJ/mol	NIST
ΔvapH°	26.40	kJ/mol	NIST
ΔvapH°	26.42	kJ/mol	NIST
ΔvapH°	Outlier 27.40	kJ/mol	NIST
ΔvapH°	26.20	kJ/mol	NIST
IE	[10.18; 10.93]	eV
IE	10.28 ± 0.10	eV	NIST
IE	10.37	eV	NIST
IE	10.43	eV	NIST
IE	10.22 ± 0.05	eV	NIST
IE	10.28 ± 0.10	eV	NIST
IE	10.18 ± 0.15	eV	NIST
IE	Outlier 10.93	eV	NIST
IE	10.20 ± 0.10	eV	NIST
IE	10.50	eV	NIST
IE	10.36	eV	NIST
IE	10.59 ± 0.05	eV	NIST
IE	10.37	eV	NIST
IE	10.35	eV	NIST
IE	Outlier 10.90 ± 0.10	eV	NIST
log10WS	[-3.18; -3.18]
log10WS	-3.18		Aq. Solubility Prediction
log10WS	-3.18		Estimated Solubility
logPoct/wat	3.390		NCMS SOLV-DB
McVol	81.310	ml/mol	McGowan Calculated Property
NFPA Fire	[%!d(float64=4); %!d(float64=4)]
NFPA Fire	4		KDB
NFPA Fire	4		NCMS SOLV-DB
NFPA Health	[%!d(float64=1); %!d(float64=1)]
NFPA Health	1		KDB
NFPA Health	1		NCMS SOLV-DB
NFPA Safety	0		NCMS SOLV-DB
Pc	[3268.00; 3406.01]	kPa
Pc	3370.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 2 Compiled value
Pc	3369.06	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	3368.78	kPa	Passut and Danner (1973), critical constants and acentric factors Compiled value
Pc	3370.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	3370.00	kPa	KDB
Pc	3370.00 ± 20.00	kPa	NIST
Pc	3369.00 ± 20.00	kPa	NIST
Pc	3360.00 ± 40.00	kPa	NIST
Pc	3330.00 ± 50.00	kPa	NIST
Pc	3370.00 ± 30.00	kPa	NIST
Pc	3360.00 ± 10.00	kPa	NIST
Pc	3360.00 ± 20.00	kPa	NIST
Pc	3369.00 ± 20.00	kPa	NIST
Pc	3369.00	kPa	NIST
Pc	3382.00 ± 5.00	kPa	NIST
Pc	3363.80 ± 0.33	kPa	NIST
Pc	3364.00	kPa	NIST
Pc	3380.00 ± 20.00	kPa	NIST
Pc	3378.00 ± 3.37	kPa	NIST
Pc	Outlier 3268.00 ± 101.33	kPa	NIST
Pc	3376.35 ± 20.68	kPa	NIST
Pc	3375.14 ± 6.07	kPa	NIST
Pc	3406.01 ± 20.68	kPa	NIST
Pc	3346.40 ± 66.70	kPa	NIST
Pc	Outlier 3270.00 ± 196.13	kPa	NIST
Ptriple	6.86e-05	kPa	ChemSep v8.3 pure component data Compiled value
ρc	[229.22; 236.65]	kg/m3
ρc	232.32 ± 1.44	kg/m3	NIST
ρc	229.22 ± 4.33	kg/m3	NIST
ρc	230.52 ± 4.33	kg/m3	NIST
ρc	230.15 ± 10.10	kg/m3	NIST
ρc	230.15 ± 5.77	kg/m3	NIST
ρc	236.65 ± 5.77	kg/m3	NIST
ρc	236.65	kg/m3	NIST
ρc	232.32 ± 2.31	kg/m3	NIST
ρc	232.32 ± 5.05	kg/m3	NIST
ρc	230.88 ± 2.89	kg/m3	NIST
ρc	236.65 ± 5.77	kg/m3	NIST
ρc	232.32 ± 2.89	kg/m3	NIST
ρc	232.32 ± 2.16	kg/m3	NIST
ρc	232.32 ± 5.77	kg/m3	NIST
S°gas	347.82 ± 0.84	J/mol×K	NIST
S°liquid	[259.40; 263.47]	J/mol×K
S°liquid	263.47	J/mol×K	NIST
S°liquid	262.67	J/mol×K	NIST
S°liquid	259.40	J/mol×K	NIST
Tboil	[301.00; 311.15]	K
Tboil	309.30	K	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Tboil	309.22	K	ChemSep v8.3 pure component data Compiled value
Tboil	309.21	K	KDB
Tboil	309.21	K	NCMS SOLV-DB
Tboil	309.30	K	NIST
Tboil	309.20	K	NIST
Tboil	309.29 ± 0.20	K	NIST
Tboil	309.15 ± 0.30	K	NIST
Tboil	309.20 ± 0.07	K	NIST
Tboil	308.40 ± 2.00	K	NIST
Tboil	309.22 ± 0.10	K	NIST
Tboil	309.19 ± 0.10	K	NIST
Tboil	309.10 ± 0.20	K	NIST
Tboil	309.25 ± 0.50	K	NIST
Tboil	309.20 ± 0.10	K	NIST
Tboil	309.15 ± 0.20	K	NIST
Tboil	309.10 ± 0.20	K	NIST
Tboil	309.30 ± 0.30	K	NIST
Tboil	309.06 ± 0.30	K	NIST
Tboil	309.30 ± 0.20	K	NIST
Tboil	309.35 ± 0.20	K	NIST
Tboil	309.25 ± 0.30	K	NIST
Tboil	310.25 ± 2.00	K	NIST
Tboil	309.15 ± 1.00	K	NIST
Tboil	309.22 ± 0.20	K	NIST
Tboil	309.30 ± 0.10	K	NIST
Tboil	309.30 ± 0.20	K	NIST
Tboil	309.15 ± 0.50	K	NIST
Tboil	309.25 ± 0.30	K	NIST
Tboil	309.10 ± 0.10	K	NIST
Tboil	309.22 ± 0.05	K	NIST
Tboil	309.30 ± 0.50	K	NIST
Tboil	309.30 ± 0.30	K	NIST
Tboil	309.30 ± 0.50	K	NIST
Tboil	309.15 ± 2.00	K	NIST
Tboil	309.21 ± 0.10	K	NIST
Tboil	309.22 ± 0.01	K	NIST
Tboil	309.25 ± 1.00	K	NIST
Tboil	309.30 ± 0.10	K	NIST
Tboil	309.30 ± 0.10	K	NIST
Tboil	309.15 ± 0.50	K	NIST
Tboil	309.22 ± 0.20	K	NIST
Tboil	309.55 ± 2.00	K	NIST
Tboil	309.15 ± 0.50	K	NIST
Tboil	309.20 ± 0.20	K	NIST
Tboil	309.15 ± 0.20	K	NIST
Tboil	309.30 ± 0.20	K	NIST
Tboil	309.05 ± 0.50	K	NIST
Tboil	309.10 ± 0.20	K	NIST
Tboil	309.15 ± 0.10	K	NIST
Tboil	309.25 ± 0.50	K	NIST
Tboil	309.45 ± 0.50	K	NIST
Tboil	308.65 ± 1.00	K	NIST
Tboil	309.15 ± 0.50	K	NIST
Tboil	309.10 ± 0.15	K	NIST
Tboil	309.15 ± 0.20	K	NIST
Tboil	309.15 ± 1.00	K	NIST
Tboil	308.15 ± 2.00	K	NIST
Tboil	308.65 ± 1.00	K	NIST
Tboil	309.05 ± 0.50	K	NIST
Tboil	309.30 ± 0.10	K	NIST
Tboil	309.40 ± 0.50	K	NIST
Tboil	309.15 ± 1.00	K	NIST
Tboil	309.22 ± 0.05	K	NIST
Tboil	309.55 ± 2.00	K	NIST
Tboil	309.25 ± 0.07	K	NIST
Tboil	309.20 ± 0.50	K	NIST
Tboil	309.65 ± 1.00	K	NIST
Tboil	309.35 ± 0.50	K	NIST
Tboil	309.21 ± 0.07	K	NIST
Tboil	309.05 ± 0.50	K	NIST
Tboil	309.15 ± 1.00	K	NIST
Tboil	309.30 ± 0.30	K	NIST
Tboil	309.15 ± 0.10	K	NIST
Tboil	309.30 ± 0.20	K	NIST
Tboil	308.95 ± 1.00	K	NIST
Tboil	309.00 ± 1.00	K	NIST
Tboil	309.00 ± 1.00	K	NIST
Tboil	309.35 ± 0.30	K	NIST
Tboil	310.15 ± 0.60	K	NIST
Tboil	309.16 ± 0.20	K	NIST
Tboil	310.15 ± 0.50	K	NIST
Tboil	309.30 ± 0.50	K	NIST
Tboil	309.30 ± 0.20	K	NIST
Tboil	309.10 ± 1.00	K	NIST
Tboil	310.65 ± 2.00	K	NIST
Tboil	309.50 ± 1.00	K	NIST
Tboil	309.50 ± 0.50	K	NIST
Tboil	309.45 ± 0.50	K	NIST
Tboil	310.65 ± 1.50	K	NIST
Tboil	309.30 ± 0.30	K	NIST
Tboil	309.30 ± 0.30	K	NIST
Tboil	309.30 ± 0.30	K	NIST
Tboil	Outlier 311.15 ± 2.00	K	NIST
Tboil	310.15 ± 1.00	K	NIST
Tboil	309.45 ± 0.50	K	NIST
Tboil	Outlier 301.00 ± 2.00	K	NIST
Tboil	309.40 ± 1.00	K	NIST
Tboil	309.40 ± 1.00	K	NIST
Tc	[460.30; 470.70]	K
Tc	469.70	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 2 Compiled value
Tc	469.70	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	469.65	K	Passut and Danner (1973), critical constants and acentric factors Compiled value
Tc	469.70	K	ChemSep v8.3 pure component data Compiled value
Tc	469.70	K	KDB
Tc	469.70 ± 0.20	K	NIST
Tc	469.68 ± 0.20	K	NIST
Tc	469.70 ± 0.20	K	NIST
Tc	466.50 ± 2.00	K	NIST
Tc	466.30 ± 4.00	K	NIST
Tc	469.74 ± 0.40	K	NIST
Tc	469.60 ± 1.00	K	NIST
Tc	469.70 ± 0.40	K	NIST
Tc	469.70 ± 0.30	K	NIST
Tc	469.51 ± 0.40	K	NIST
Tc	469.70	K	NIST
Tc	469.70	K	NIST
Tc	469.69 ± 0.04	K	NIST
Tc	469.69 ± 0.10	K	NIST
Tc	469.60	K	NIST
Tc	469.80 ± 0.20	K	NIST
Tc	470.40 ± 0.04	K	NIST
Tc	469.60 ± 0.20	K	NIST
Tc	469.70 ± 0.30	K	NIST
Tc	469.70 ± 0.20	K	NIST
Tc	469.70 ± 0.30	K	NIST
Tc	469.70 ± 0.30	K	NIST
Tc	469.61 ± 0.40	K	NIST
Tc	469.75 ± 0.25	K	NIST
Tc	469.49 ± 0.20	K	NIST
Tc	469.55 ± 0.10	K	NIST
Tc	470.70 ± 1.00	K	NIST
Tc	469.77 ± 0.06	K	NIST
Tc	470.37 ± 1.11	K	NIST
Tc	470.40 ± 1.00	K	NIST
Tc	Outlier 460.30 ± 10.00	K	NIST
Tfus	[75.40; 144.15]	K
Tfus	143.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	143.42	K	ChemSep v8.3 pure component data Compiled value
Tfus	143.40	K	KDB
Tfus	143.26	K	Aq. Solubility Prediction
Tfus	143.42	K	NCMS SOLV-DB
Tfus	143.42 ± 0.02	K	NIST
Tfus	Outlier 75.40 ± 0.15	K	NIST
Tfus	143.15 ± 1.50	K	NIST
Tfus	144.05 ± 0.40	K	NIST
Tfus	143.42 ± 0.30	K	NIST
Tfus	143.43 ± 0.15	K	NIST
Tfus	143.40 ± 0.10	K	NIST
Tfus	143.40 ± 0.30	K	NIST
Tfus	143.41 ± 0.05	K	NIST
Tfus	143.42 ± 0.03	K	NIST
Tfus	142.65 ± 0.50	K	NIST
Tfus	143.39 ± 0.06	K	NIST
Tfus	Outlier 80.42 ± 0.04	K	NIST
Tfus	143.40 ± 0.05	K	NIST
Tfus	143.39 ± 0.02	K	NIST
Tfus	143.39 ± 0.06	K	NIST
Tfus	143.42 ± 0.03	K	NIST
Tfus	143.39 ± 0.20	K	NIST
Tfus	143.48 ± 0.30	K	NIST
Tfus	143.39 ± 0.07	K	NIST
Tfus	143.42 ± 0.05	K	NIST
Tfus	143.40 ± 0.10	K	NIST
Tfus	143.45 ± 0.20	K	NIST
Tfus	143.45 ± 0.20	K	NIST
Tfus	144.15 ± 2.00	K	NIST
Tfus	144.05 ± 0.50	K	NIST
Tfus	143.00 ± 2.00	K	NIST
Tfus	144.15 ± 0.30	K	NIST
Tfus	143.42 ± 0.05	K	NIST
Tfus	143.45 ± 0.40	K	NIST
Tfus	143.22 ± 0.08	K	NIST
Tfus	142.35 ± 0.30	K	NIST
Ttriple	[143.40; 143.48]	K
Ttriple	143.48	K	Staveley, Lobo and Calado (1981), triple points Compiled value
Ttriple	143.42	K	ChemSep v8.3 pure component data Compiled value
Ttriple	143.43	K	KDB
Ttriple	143.47 ± 0.03	K	NIST
Ttriple	143.45 ± 0.07	K	NIST
Ttriple	143.48 ± 0.04	K	NIST
Ttriple	143.48 ± 0.05	K	NIST
Ttriple	143.47 ± 0.07	K	NIST
Ttriple	143.40 ± 0.30	K	NIST
UQi	3.32		ChemSep v8.3 pure component data Compiled value
URi	3.83		ChemSep v8.3 pure component data Compiled value
Vc	[0.295; 0.315]	m3/kmol
Vc	0.311	m3/kmol	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 2 Compiled value
Vc	0.304	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.311	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.311	m3/kmol	KDB
Vc	0.311	m3/kmol	NIST
Vc	0.310 ± 0.000	m3/kmol	NIST
Vc	Outlier 0.295 ± 0.006	m3/kmol	NIST
Vc	0.315 ± 0.003	m3/kmol	NIST
VCOSTALD	0.31	m3/kmol	Hankinson and Thomson (1979), COSTALD parameters Compiled value
ωSRK	0.25		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zc	[0.2680000; 0.2683690]
Zc	0.2680000		IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 2 Compiled value
Zc	0.2680000		ChemSep v8.3 pure component data Compiled value
Zc	0.2683690		KDB
Zra	[0.27; 0.27]
Zra	0.27		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zra	0.27		ChemSep v8.3 pure component data Compiled value
Zra	0.27		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[120.07; 232.90]	J/mol×K	[298.15; 700.00]
Cp,gas	120.07 ± 0.24	J/mol×K	298.15	NIST
Cp,gas	127.84 ± 0.26	J/mol×K	323.15	NIST
Cp,gas	135.90 ± 0.27	J/mol×K	348.15	NIST
Cp,gas	143.95 ± 0.29	J/mol×K	373.15	NIST
Cp,gas	151.92 ± 0.30	J/mol×K	398.15	NIST
Cp,gas	159.67 ± 0.32	J/mol×K	423.15	NIST
Cp,gas	167.37 ± 0.33	J/mol×K	448.15	NIST
Cp,gas	168.11	J/mol×K	450.00	NIST
Cp,gas	174.75 ± 0.35	J/mol×K	473.15	NIST
Cp,gas	181.98 ± 0.36	J/mol×K	498.15	NIST
Cp,gas	182.39	J/mol×K	500.00	NIST
Cp,gas	189.08 ± 0.38	J/mol×K	523.15	NIST
Cp,gas	195.96	J/mol×K	550.00	NIST
Cp,gas	209.23	J/mol×K	600.00	NIST
Cp,gas	221.93	J/mol×K	650.00	NIST
Cp,gas	232.90	J/mol×K	700.00	NIST
Cp,liquid	[141.60; 204.40]	J/mol×K	[150.00; 390.00]
Cp,liquid	141.60	J/mol×K	150.00	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	141.60	J/mol×K	160.00	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	141.90	J/mol×K	170.00	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	142.50	J/mol×K	180.00	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	143.30	J/mol×K	190.00	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	144.40	J/mol×K	200.00	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	145.70	J/mol×K	210.00	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	147.30	J/mol×K	220.00	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	149.20	J/mol×K	230.00	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	151.20	J/mol×K	240.00	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	153.60	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	156.10	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	158.80	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	159.70	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	161.70	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	164.70	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	163.20	J/mol×K	290.00	NIST
Cp,liquid	167.99	J/mol×K	290.00	NIST
Cp,liquid	168.60	J/mol×K	298.00	NIST
Cp,liquid	167.30	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	167.19	J/mol×K	298.15	NIST
Cp,liquid	167.90	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	171.30	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	174.80	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	178.50	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	182.30	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	186.40	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	190.60	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	195.00	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	199.60	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	204.40	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
η	0.0002250	Pa×s	298.15	NCMS SOLV-DB
ΔfusH	[8.38; 8.41]	kJ/mol	[143.40; 143.50]
ΔfusH	8.38	kJ/mol	143.40	NIST
ΔfusH	8.41	kJ/mol	143.46	NIST
ΔfusH	8.40	kJ/mol	143.47	NIST
ΔfusH	8.40	kJ/mol	143.50	NIST
ΔfusH	8.40	kJ/mol	143.50	NIST
ΔsubH	42.00	kJ/mol	143.00	NIST
ΔvapH	[8.50; 32.30]	kJ/mol	[183.00; 460.00]
ΔvapH	32.30	kJ/mol	183.00	NIST
ΔvapH	29.80	kJ/mol	287.50	NIST
ΔvapH	26.20	kJ/mol	298.15	NIST
ΔvapH	27.90	kJ/mol	305.00	NIST
ΔvapH	25.79	kJ/mol	309.20	NIST
ΔvapH	25.77	kJ/mol	309.20	KDB
ΔvapH	25.50	kJ/mol	310.00	NIST
ΔvapH	23.00	kJ/mol	350.00	NIST
ΔvapH	26.70	kJ/mol	365.50	NIST
ΔvapH	26.10	kJ/mol	386.00	NIST
ΔvapH	19.70	kJ/mol	390.00	NIST
ΔvapH	15.10	kJ/mol	430.00	NIST
ΔvapH	26.20	kJ/mol	444.00	NIST
ΔvapH	8.50	kJ/mol	460.00	NIST
Pvap	[48.00; 3286.00]	kPa	[288.25; 468.15]
Pvap	48.00	kPa	288.25	Isothermal Vapor-Liquid Equilibrium Data for Binary Mixtures of Hexafluoroethane (R116) + n-Pentane or n-Hexane at Two Temperatures, 288 and 296 K
Pvap	66.00	kPa	296.24	Isothermal Vapor-Liquid Equilibrium Data for Binary Mixtures of Hexafluoroethane (R116) + n-Pentane or n-Hexane at Two Temperatures, 288 and 296 K
Pvap	68.33	kPa	298.15	NCMS SOLV-DB
Pvap	101.32	kPa	309.30	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	101.73	kPa	309.32	Vapour pressures of n-pentane determined by comparative ebulliometry
Pvap	118.39	kPa	313.85	Vapour pressures of n-pentane determined by comparative ebulliometry
Pvap	145.30	kPa	320.20	Vapour pressures of n-pentane determined by comparative ebulliometry
Pvap	169.71	kPa	325.22	Vapour pressures of n-pentane determined by comparative ebulliometry
Pvap	200.67	kPa	330.84	Vapour pressures of n-pentane determined by comparative ebulliometry
Pvap	215.21	kPa	333.15	Vapor Liquid Equilibrium for Several Compounds Relevant to the Biofuels Industry Modeled with the Wilson Equation
Pvap	227.66	kPa	335.22	Vapour pressures of n-pentane determined by comparative ebulliometry
Pvap	256.78	kPa	339.51	Vapour pressures of n-pentane determined by comparative ebulliometry
Pvap	284.81	kPa	343.32	Vapour pressures of n-pentane determined by comparative ebulliometry
Pvap	312.35	kPa	346.78	Vapour pressures of n-pentane determined by comparative ebulliometry
Pvap	338.98	kPa	349.92	Vapour pressures of n-pentane determined by comparative ebulliometry
Pvap	371.25	kPa	353.48	Vapour pressures of n-pentane determined by comparative ebulliometry
Pvap	403.22	kPa	356.79	Vapour pressures of n-pentane determined by comparative ebulliometry
Pvap	436.34	kPa	360.01	Vapour pressures of n-pentane determined by comparative ebulliometry
Pvap	471.57	kPa	363.24	Vapour pressures of n-pentane determined by comparative ebulliometry
Pvap	507.70	kPa	366.37	Vapour pressures of n-pentane determined by comparative ebulliometry
Pvap	551.11	kPa	369.92	Vapour pressures of n-pentane determined by comparative ebulliometry
Pvap	600.00	kPa	373.15	In Situ Determination of Phase Equilibria of Methyl Benzoate + Alkane Mixtures Using an Infrared Absorption Method. Comparison with Polar GC-SAFT Predictions
Pvap	648.59	kPa	377.19	Vapour pressures of n-pentane determined by comparative ebulliometry
Pvap	754.18	kPa	384.19	Vapour pressures of n-pentane determined by comparative ebulliometry
Pvap	895.85	kPa	392.52	Vapour pressures of n-pentane determined by comparative ebulliometry
Pvap	917.75	kPa	393.15	Vapor Liquid Equilibrium for Several Compounds Relevant to the Biofuels Industry Modeled with the Wilson Equation
Pvap	995.29	kPa	397.80	Vapour pressures of n-pentane determined by comparative ebulliometry
Pvap	1092.40	kPa	402.59	Vapour pressures of n-pentane determined by comparative ebulliometry
Pvap	1185.12	kPa	406.87	Vapour pressures of n-pentane determined by comparative ebulliometry
Pvap	1300.00	kPa	406.90	Experimental High-Pressure Isochoric/Isoplethic Equilibrium for the Systems Propane + n-Pentane and Propane + Diethyl Ether
Pvap	1317.45	kPa	412.57	Vapour pressures of n-pentane determined by comparative ebulliometry
Pvap	1405.53	kPa	416.13	Vapour pressures of n-pentane determined by comparative ebulliometry
Pvap	1450.02	kPa	417.87	Vapour pressures of n-pentane determined by comparative ebulliometry
Pvap	1508.64	kPa	420.09	Vapour pressures of n-pentane determined by comparative ebulliometry
Pvap	1620.00	kPa	423.15	In Situ Determination of Phase Equilibria of Methyl Benzoate + Alkane Mixtures Using an Infrared Absorption Method. Comparison with Polar GC-SAFT Predictions
Pvap	1608.88	kPa	423.75	Vapour pressures of n-pentane determined by comparative ebulliometry
Pvap	1633.21	kPa	424.62	Vapour pressures of n-pentane determined by comparative ebulliometry
Pvap	1704.41	kPa	427.09	Vapour pressures of n-pentane determined by comparative ebulliometry
Pvap	1804.83	kPa	430.44	Vapour pressures of n-pentane determined by comparative ebulliometry
Pvap	1812.00	kPa	430.68	Vapour pressures of n-pentane determined by comparative ebulliometry
Pvap	1903.73	kPa	433.61	Vapour pressures of n-pentane determined by comparative ebulliometry
Pvap	2033.22	kPa	437.57	Vapour pressures of n-pentane determined by comparative ebulliometry
Pvap	2143.72	kPa	440.81	Vapour pressures of n-pentane determined by comparative ebulliometry
Pvap	2242.61	kPa	443.59	Vapour pressures of n-pentane determined by comparative ebulliometry
Pvap	2355.20	kPa	446.65	Vapour pressures of n-pentane determined by comparative ebulliometry
Pvap	2451.91	kPa	449.18	Vapour pressures of n-pentane determined by comparative ebulliometry
Pvap	2559.30	kPa	451.90	Vapour pressures of n-pentane determined by comparative ebulliometry
Pvap	2562.84	kPa	451.99	Vapour pressures of n-pentane determined by comparative ebulliometry
Pvap	2658.58	kPa	454.33	Vapour pressures of n-pentane determined by comparative ebulliometry
Pvap	2727.72	kPa	455.99	Vapour pressures of n-pentane determined by comparative ebulliometry
Pvap	3286.00	kPa	468.15	Isothermal Vapor-Liquid Equilibria for the n-Pentane + 1-Butanol and n-Pentane + 2-Butanol Systems near the Critical Region of the Mixtures
n0	[1.35230; 1.35870]		[293.15; 303.15]
n0	1.35780		293.15	Isobaric Vapor Liquid Equilibrium for Nine Binary Systems of Cracking C5 Fraction at 250 kPa
n0	1.35870		298.10	Excess Enthalpies and Thermal Conductivity Coefficients for Binary Mixtures of Carbon Tetrachloride and Four Alkanes (C5 to C8) at a Temperature of 298.15 K
n0	1.35450		298.15	Multiproperty Correlation of Experimental Data of the Binaries Propyl Ethanoate + Alkanes (Pentane to Decane). New Experimental Information for Vapor Liquid Equilibrium and Mixing Properties
n0	1.35470		298.15	Improvements in the Experimentation and the Representation of Thermodynamic Properties (iso-p VLE and yE) of Alkyl Propanoate + Alkane Binaries
n0	1.35472		298.15	KDB
n0	1.35500		298.15	NCMS SOLV-DB
n0	1.35230		303.15	Phase equilibria measurements of ternary mixtures (sulfolane + a carboxylic acid + pentane) at 303.15 K
ρl	[611.01; 645.50]	kg/m3	[273.15; 308.15]
ρl	645.50	kg/m3	273.15	Experimental measurements and prediction of liquid densities for n-alkane mixtures
ρl	640.70	kg/m3	278.15	Experimental measurements and prediction of liquid densities for n-alkane mixtures
ρl	635.90	kg/m3	283.15	Experimental measurements and prediction of liquid densities for n-alkane mixtures
ρl	631.04	kg/m3	288.15	Experimental measurements and prediction of liquid densities for n-alkane mixtures
ρl	627.86	kg/m3	291.15	Experimentation and thermodynamic representations of binaries containing compounds of low boiling points: Pentane and alkylmethanoates
ρl	626.00	kg/m3	293.00	KDB
ρl	627.00	kg/m3	293.15	Experimental Phase Equilibrium for the Binary System of n-Pentane +2-Propanol Using a New Equilibrium Cell and the Static Total Pressure Method
ρl	626.23	kg/m3	293.15	Surface tension and density of mixtures of m-xylene + n-alkane at 293.15 K: Analysis under the extended Langmuir and Shereshefsky models
ρl	626.12	kg/m3	293.15	Experimental measurements and prediction of liquid densities for n-alkane mixtures
ρl	626.00	kg/m3	293.15	Total Pressure Phase Equilibrium Measurements for the Binary Systems of n-Pentane + Cyclohexane and 1-Hexene + 2-Propanol
ρl	621.14	kg/m3	298.15	Experimental measurements and prediction of liquid densities for n-alkane mixtures
ρl	621.22	kg/m3	298.15	Excess molar volumes and dynamic viscosities for binary mixtures of toluene + n-alkanes (C5 C10) at T = 298.15 K Comparison with Prigogine Flory Patterson theory
ρl	621.30	kg/m3	298.15	Liquid-Liquid Equilibrium Data for Ternary Systems Containing Alkanes (n-Pentane, n-Hexane, n-Heptane, and n-Octane) + Alcohol (Methanol and Ethanol) + Protic Ionic Liquid (2-HEAF)
ρl	621.32	kg/m3	298.15	Viscosities and Excess Molar Volumes of the Ternary System Toluene (1) + Cyclohexane (2) + Pentane (3) at 298.15 K
ρl	620.89	kg/m3	298.15	Experimentation and thermodynamic representations of binaries containing compounds of low boiling points: Pentane and alkylmethanoates
ρl	624.93	kg/m3	298.20	Apparent and Partial Molar Volumes at Infinite Dilution and Solid Liquid Equilibria of Dibenzothiophene + Alkane Systems
ρl	616.11	kg/m3	303.15	Experimental measurements and prediction of liquid densities for n-alkane mixtures
ρl	611.01	kg/m3	308.15	Experimental measurements and prediction of liquid densities for n-alkane mixtures
ΔfusS	[58.41; 58.66]	J/mol×K	[143.40; 143.47]
ΔfusS	58.41	J/mol×K	143.40	NIST
ΔfusS	58.66	J/mol×K	143.46	NIST
ΔfusS	58.56	J/mol×K	143.47	NIST
γ	[0.01; 0.02]	N/m	[293.15; 323.15]
γ	0.02	N/m	293.15	Experimental and theoretical study of surface tension of n-pentane, n-heptane, and some of their mixtures at different temperatures
γ	0.02	N/m	293.20	KDB
γ	0.02	N/m	298.15	Experimental and theoretical study of surface tension of n-pentane, n-heptane, and some of their mixtures at different temperatures
γ	0.02	N/m	298.15	NCMS SOLV-DB
γ	0.01	N/m	305.15	Experimental and theoretical study of surface tension of n-pentane, n-heptane, and some of their mixtures at different temperatures
γ	0.01	N/m	318.15	Experimental and theoretical study of surface tension of n-pentane, n-heptane, and some of their mixtures at different temperatures
γ	0.01	N/m	323.15	Experimental and theoretical study of surface tension of n-pentane, n-heptane, and some of their mixtures at different temperatures
ΔvapS	87.88	J/mol×K	298.15	NIST
αdiff	[2.59e-08; 7.18e-08]	m2/s	[306.16; 466.37]
αdiff	7.18e-08	m2/s	306.16	Thermal Diffusivity and Speed of Sound of Saturated Pentane from Light Scattering
αdiff	6.84e-08	m2/s	323.16	Thermal Diffusivity and Speed of Sound of Saturated Pentane from Light Scattering
αdiff	6.42e-08	m2/s	338.39	Thermal Diffusivity and Speed of Sound of Saturated Pentane from Light Scattering
αdiff	6.19e-08	m2/s	353.16	Thermal Diffusivity and Speed of Sound of Saturated Pentane from Light Scattering
αdiff	6.07e-08	m2/s	358.13	Thermal Diffusivity and Speed of Sound of Saturated Pentane from Light Scattering
αdiff	5.91e-08	m2/s	362.37	Thermal Diffusivity and Speed of Sound of Saturated Pentane from Light Scattering
αdiff	5.79e-08	m2/s	368.18	Thermal Diffusivity and Speed of Sound of Saturated Pentane from Light Scattering
αdiff	5.74e-08	m2/s	373.47	Thermal Diffusivity and Speed of Sound of Saturated Pentane from Light Scattering
αdiff	5.69e-08	m2/s	378.20	Thermal Diffusivity and Speed of Sound of Saturated Pentane from Light Scattering
αdiff	5.53e-08	m2/s	383.42	Thermal Diffusivity and Speed of Sound of Saturated Pentane from Light Scattering
αdiff	5.45e-08	m2/s	388.15	Thermal Diffusivity and Speed of Sound of Saturated Pentane from Light Scattering
αdiff	5.40e-08	m2/s	393.32	Thermal Diffusivity and Speed of Sound of Saturated Pentane from Light Scattering
αdiff	5.35e-08	m2/s	396.29	Thermal Diffusivity and Speed of Sound of Saturated Pentane from Light Scattering
αdiff	5.24e-08	m2/s	399.16	Thermal Diffusivity and Speed of Sound of Saturated Pentane from Light Scattering
αdiff	5.16e-08	m2/s	403.33	Thermal Diffusivity and Speed of Sound of Saturated Pentane from Light Scattering
αdiff	5.12e-08	m2/s	408.63	Thermal Diffusivity and Speed of Sound of Saturated Pentane from Light Scattering
αdiff	5.01e-08	m2/s	413.33	Thermal Diffusivity and Speed of Sound of Saturated Pentane from Light Scattering
αdiff	4.93e-08	m2/s	418.39	Thermal Diffusivity and Speed of Sound of Saturated Pentane from Light Scattering
αdiff	4.84e-08	m2/s	423.61	Thermal Diffusivity and Speed of Sound of Saturated Pentane from Light Scattering
αdiff	4.69e-08	m2/s	428.17	Thermal Diffusivity and Speed of Sound of Saturated Pentane from Light Scattering
αdiff	4.58e-08	m2/s	433.29	Thermal Diffusivity and Speed of Sound of Saturated Pentane from Light Scattering
αdiff	4.49e-08	m2/s	436.19	Thermal Diffusivity and Speed of Sound of Saturated Pentane from Light Scattering
αdiff	4.43e-08	m2/s	439.21	Thermal Diffusivity and Speed of Sound of Saturated Pentane from Light Scattering
αdiff	4.38e-08	m2/s	442.35	Thermal Diffusivity and Speed of Sound of Saturated Pentane from Light Scattering
αdiff	4.34e-08	m2/s	445.16	Thermal Diffusivity and Speed of Sound of Saturated Pentane from Light Scattering
αdiff	4.20e-08	m2/s	448.08	Thermal Diffusivity and Speed of Sound of Saturated Pentane from Light Scattering
αdiff	4.08e-08	m2/s	451.38	Thermal Diffusivity and Speed of Sound of Saturated Pentane from Light Scattering
αdiff	3.84e-08	m2/s	455.20	Thermal Diffusivity and Speed of Sound of Saturated Pentane from Light Scattering
αdiff	3.55e-08	m2/s	458.40	Thermal Diffusivity and Speed of Sound of Saturated Pentane from Light Scattering
αdiff	3.37e-08	m2/s	460.10	Thermal Diffusivity and Speed of Sound of Saturated Pentane from Light Scattering
αdiff	3.04e-08	m2/s	463.41	Thermal Diffusivity and Speed of Sound of Saturated Pentane from Light Scattering
αdiff	2.59e-08	m2/s	466.37	Thermal Diffusivity and Speed of Sound of Saturated Pentane from Light Scattering

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboil(P)	309.15	K	96.60	Low cost apparatus for rapid boiling point determination of small air sensitive samples under inert atmosphere

Datasets

1. Mass density, kg/m3 (1)
2. Thermal conductivity, W/m/K (1)
3. Thermal conductivity, W/m/K (1)

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.21	2000.00	628.05
293.21	3998.00	630.31
293.21	6000.00	632.63
293.21	8003.00	634.89
293.22	10008.00	636.91
293.21	13008.00	640.02
293.22	16007.00	643.0
293.22	19009.00	645.81
293.22	22010.00	648.59
293.22	25002.00	651.19
293.22	28002.00	653.72
293.21	30000.00	655.38
313.10	2005.00	608.49
313.11	4002.00	611.31
313.10	6001.00	613.99
313.10	7999.00	616.58
313.10	10005.00	619.09
313.10	13001.00	622.65
313.10	16005.00	626.03
313.10	19002.00	629.28
313.10	22002.00	632.38
313.10	25004.00	635.4
313.10	28002.00	638.2
313.10	30005.00	640.09
333.01	2009.00	587.87
333.01	3997.00	591.4
333.01	6002.00	594.59
333.01	8008.00	597.69
333.01	10001.00	600.61
333.01	12998.00	604.82
333.01	15996.00	608.78
333.01	19000.00	612.5
333.01	21997.00	616.1
333.01	25000.00	619.39
333.01	27997.00	622.68
333.01	30006.00	624.71
353.12	2006.00	565.77
353.12	3997.00	570.01
353.12	6002.00	574.02
353.12	8003.00	577.79
353.12	10008.00	581.28
353.12	13000.00	586.31
353.12	16001.00	590.9
353.12	18997.00	595.21
353.13	22000.00	599.29
353.12	25002.00	603.1
353.12	28005.00	606.77
353.12	30001.00	609.1
Reference

Thermal conductivity, W/m/K

Fixed		Measured
Temperature, K - Gas	Pressure, kPa - Gas	Thermal conductivity, W/m/K - Gas
342.97	100.00	0.0189
366.02	100.00	0.0217
380.86	100.00	0.0237
407.37	100.00	0.0272
342.97	200.00	0.0190
366.02	200.00	0.0218
380.86	200.00	0.0238
407.37	200.00	0.0273
342.97	500.00	0.0192
366.02	500.00	0.0220
380.86	500.00	0.0240
407.37	500.00	0.0275
Reference

Thermal conductivity, W/m/K

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Thermal conductivity, W/m/K - Liquid
309.04	260.00	0.1090
309.04	261.00	0.1092
309.04	1000.00	0.1095
309.04	2000.00	0.1101
309.04	3012.00	0.1108
309.04	4151.00	0.1118
309.04	4297.00	0.1117
309.04	5604.00	0.1123
309.04	6001.00	0.1125
309.04	7000.00	0.1130
309.04	8108.00	0.1137
309.04	9011.00	0.1142
309.04	10008.00	0.1154
309.04	11054.00	0.1161
309.04	12000.00	0.1167
309.04	12504.00	0.1168
309.04	13000.00	0.1171
309.04	14742.00	0.1181
309.04	19800.00	0.1207
309.04	19908.00	0.1205
309.04	20004.00	0.1206
309.04	24000.00	0.1231
309.04	25000.00	0.1233
309.04	28000.00	0.1241
309.04	29100.00	0.1253
309.04	29300.00	0.1256
309.04	34000.00	0.1281
309.04	35000.00	0.1286
309.04	38000.00	0.1298
309.04	39100.00	0.1299
309.04	39176.00	0.1300
309.04	39350.00	0.1304
309.04	49940.00	0.1352
309.04	50230.00	0.1353
309.04	50800.00	0.1352
331.20	2097.00	0.1035
331.20	3000.00	0.1041
331.20	3500.00	0.1045
331.20	4000.00	0.1046
331.20	5000.00	0.1053
331.20	6000.00	0.1061
331.20	7000.00	0.1068
331.20	8000.00	0.1069
331.20	9000.00	0.1072
331.20	9500.00	0.1077
331.20	10000.00	0.1078
331.20	11000.00	0.1085
331.20	12000.00	0.1090
331.20	13000.00	0.1094
331.20	15000.00	0.1109
331.20	16000.00	0.1115
331.20	17000.00	0.1122
331.20	18000.00	0.1126
331.20	19000.00	0.1131
331.20	20000.00	0.1139
331.20	21000.00	0.1141
331.20	22000.00	0.1148
331.20	24000.00	0.1158
331.20	25482.00	0.1167
331.20	26404.00	0.1172
331.20	27000.00	0.1176
331.20	30000.00	0.1188
331.20	31040.00	0.1193
331.20	31081.00	0.1193
331.20	32500.00	0.1202
331.20	32500.00	0.1202
331.20	33500.00	0.1209
331.20	34477.00	0.1211
331.20	35500.00	0.1216
331.20	36500.00	0.1224
331.20	37885.00	0.1229
331.20	38500.00	0.1231
331.20	39000.00	0.1237
331.20	39500.00	0.1239
331.20	40000.00	0.1241
331.20	41000.00	0.1242
331.20	42000.00	0.1246
331.20	43500.00	0.1255
331.20	44500.00	0.1261
331.20	45500.00	0.1266
331.20	47000.00	0.1272
331.20	48000.00	0.1273
331.20	49500.00	0.1283
331.20	50000.00	0.1278
386.00	5061.00	0.0901
386.00	10175.00	0.0945
386.00	18875.00	0.0996
386.00	20275.00	0.1023
386.00	30275.00	0.1082
386.00	34475.00	0.1107
386.00	40275.00	0.1122
386.00	49975.00	0.1184
386.00	53475.00	0.1203
399.60	2900.00	0.0846
399.60	3000.00	0.0849
399.60	4000.00	0.0852
399.60	4500.00	0.0860
399.60	5000.00	0.0869
399.60	6000.00	0.0880
399.60	7000.00	0.0890
399.60	7500.00	0.0895
399.60	8000.00	0.0899
399.60	9500.00	0.0913
399.60	10000.00	0.0917
399.60	11000.00	0.0924
399.60	12000.00	0.0932
399.60	13000.00	0.0937
399.60	14000.00	0.0946
399.60	15000.00	0.0952
399.60	16000.00	0.0960
399.60	17000.00	0.0967
399.60	18000.00	0.0974
399.60	19000.00	0.0984
399.60	20000.00	0.0989
399.60	21000.00	0.0995
399.60	22000.00	0.1001
399.60	23500.00	0.1011
399.60	25000.00	0.1022
399.60	26000.00	0.1026
399.60	27000.00	0.1031
399.60	28000.00	0.1037
399.60	29000.00	0.1047
399.60	30000.00	0.1051
399.60	31000.00	0.1056
399.60	33000.00	0.1066
399.60	34000.00	0.1071
399.60	35000.00	0.1076
399.60	35301.00	0.1079
421.85	1640.00	0.0757
421.85	1650.00	0.0757
421.85	1660.00	0.0757
421.85	1680.00	0.0757
421.85	1700.00	0.0757
421.85	1710.00	0.0757
421.85	1720.00	0.0757
421.85	1730.00	0.0760
421.85	1750.00	0.0757
421.85	1764.00	0.0757
421.85	1772.00	0.0758
421.85	1910.00	0.0762
421.85	1946.00	0.0762
421.85	1954.00	0.0762
422.20	2518.00	0.0771
422.20	5041.00	0.0809
422.20	10475.00	0.0868
422.20	18675.00	0.0935
422.20	18775.00	0.0935
422.20	20475.00	0.0941
422.20	30575.00	0.1002
422.20	30675.00	0.1007
422.20	40275.00	0.1061
422.20	48075.00	0.1104
422.20	52975.00	0.1123
465.40	9497.00	0.0779
465.40	9610.00	0.0779
465.40	9891.00	0.0781
467.36	11000.00	0.0807
467.36	11500.00	0.0813
467.36	12000.00	0.0818
467.36	13000.00	0.0828
467.36	13800.00	0.0836
467.36	15200.00	0.0849
467.36	16000.00	0.0855
467.36	16500.00	0.0859
467.36	17000.00	0.0864
467.36	17500.00	0.0867
467.36	18000.00	0.0872
467.36	18500.00	0.0876
467.36	19000.00	0.0880
467.36	19500.00	0.0884
467.36	20000.00	0.0888
467.36	20500.00	0.0892
467.36	21000.00	0.0896
467.36	21500.00	0.0899
467.36	22000.00	0.0903
467.36	22500.00	0.0907
467.36	23000.00	0.0911
467.36	23500.00	0.0914
467.36	24000.00	0.0918
467.36	24500.00	0.0922
467.36	25000.00	0.0926
467.36	25500.00	0.0929
467.36	26000.00	0.0932
467.36	26500.00	0.0936
467.36	27000.00	0.0939
467.36	27500.00	0.0942
467.36	28000.00	0.0946
467.36	28500.00	0.0949
467.36	29000.00	0.0952
467.36	29500.00	0.0955
467.36	30000.00	0.0958
467.36	30500.00	0.0961
467.36	31000.00	0.0963
467.36	31280.00	0.0964
467.36	31300.00	0.0965
467.36	31340.00	0.0966
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[93.37; 329.56]	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			8.10620e+01
Coefficient B			-7.06860e+02
Coefficient C			6.05424e+00
Coefficient D			-4.92980e-05
Coefficient E			2.83570e-09
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	93.37	J/mol×K	200.00	Calculated Property
Cp,gas	134.87	J/mol×K	344.44	Calculated Property
Cp,gas	179.06	J/mol×K	488.89	Calculated Property
Cp,gas	216.44	J/mol×K	633.33	Calculated Property
Cp,gas	246.53	J/mol×K	777.78	Calculated Property
Cp,gas	270.62	J/mol×K	922.22	Calculated Property
Cp,gas	290.04	J/mol×K	1066.67	Calculated Property
Cp,gas	305.83	J/mol×K	1211.11	Calculated Property
Cp,gas	318.80	J/mol×K	1355.56	Calculated Property
Cp,gas	329.56	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[141.01; 204.61]	J/mol×K	[143.42; 390.00]	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			1.22980e+02
Coefficient B			4.01500e+02
Coefficient C			-2.94266e+00
Coefficient D			2.40560e-02
Coefficient E			-2.01610e-05
Temperature range, min.			143.42
Temperature range, max.			390.00
Cp,liquid	141.01	J/mol×K	143.42	Calculated Property
Cp,liquid	141.68	J/mol×K	170.82	Calculated Property
Cp,liquid	144.29	J/mol×K	198.22	Calculated Property
Cp,liquid	148.46	J/mol×K	225.61	Calculated Property
Cp,liquid	154.17	J/mol×K	253.01	Calculated Property
Cp,liquid	161.43	J/mol×K	280.41	Calculated Property
Cp,liquid	170.26	J/mol×K	307.81	Calculated Property
Cp,liquid	180.58	J/mol×K	335.20	Calculated Property
Cp,liquid	192.15	J/mol×K	362.60	Calculated Property
Cp,liquid	204.61	J/mol×K	390.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0039571; 0.0000568]	Pa×s	[137.15; 465.15]	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			-2.89385e+01
Coefficient B			1.17636e+03
Coefficient C			3.05054e+00
Coefficient D			-9.72137e-06
Coefficient E			2.00000e+00
Temperature range, min.			137.15
Temperature range, max.			465.15
η	0.0039571	Pa×s	137.15	Calculated Property
η	0.0012015	Pa×s	173.59	Calculated Property
η	0.0005788	Pa×s	210.04	Calculated Property
η	0.0003505	Pa×s	246.48	Calculated Property
η	0.0002393	Pa×s	282.93	Calculated Property
η	0.0001740	Pa×s	319.37	Calculated Property
η	0.0001306	Pa×s	355.82	Calculated Property
η	0.0000993	Pa×s	392.26	Calculated Property
η	0.0000754	Pa×s	428.71	Calculated Property
η	0.0000568	Pa×s	465.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[34.99; 1.76]	kJ/mol	[143.42; 469.50]	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			4.08540e+01
Coefficient B			2.54830e-01
Coefficient C			9.60450e-01
Coefficient D			-1.53490e+00
Coefficient E			7.25040e-01
Critical temperature, Tc (K)			4.69700e+02
Temperature range, min.			143.42
Temperature range, max.			469.50
ΔvapH	34.99	kJ/mol	143.42	Calculated Property
ΔvapH	33.07	kJ/mol	179.65	Calculated Property
ΔvapH	31.12	kJ/mol	215.88	Calculated Property
ΔvapH	29.11	kJ/mol	252.11	Calculated Property
ΔvapH	27.04	kJ/mol	288.34	Calculated Property
ΔvapH	24.80	kJ/mol	324.58	Calculated Property
ΔvapH	22.26	kJ/mol	360.81	Calculated Property
ΔvapH	19.08	kJ/mol	397.04	Calculated Property
ΔvapH	14.55	kJ/mol	433.27	Calculated Property
ΔvapH	1.76	kJ/mol	469.50	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.65]	kPa	[223.22; 330.82]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.41236e+01
Coefficient B			-2.61147e+03
Coefficient C			-3.44720e+01
Temperature range, min.			223.22
Temperature range, max.			330.82
Pvap	1.33	kPa	223.22	Calculated Property
Pvap	3.04	kPa	235.18	Calculated Property
Pvap	6.32	kPa	247.13	Calculated Property
Pvap	12.15	kPa	259.09	Calculated Property
Pvap	21.86	kPa	271.04	Calculated Property
Pvap	37.18	kPa	283.00	Calculated Property
Pvap	60.22	kPa	294.95	Calculated Property
Pvap	93.51	kPa	306.91	Calculated Property
Pvap	139.91	kPa	318.86	Calculated Property
Pvap	202.65	kPa	330.82	Calculated Property
Pvap	[6.30e-05; 3305.79]	kPa	[143.42; 469.70]	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			6.52347e+01
Coefficient B			-5.26559e+03
Coefficient C			-7.72071e+00
Coefficient D			7.15187e-06
Coefficient E			2.00000e+00
Temperature range, min.			143.42
Temperature range, max.			469.70
Pvap	6.30e-05	kPa	143.42	Calculated Property
Pvap	0.02	kPa	179.67	Calculated Property
Pvap	0.73	kPa	215.93	Calculated Property
Pvap	8.27	kPa	252.18	Calculated Property
Pvap	46.53	kPa	288.43	Calculated Property
Pvap	167.90	kPa	324.69	Calculated Property
Pvap	451.61	kPa	360.94	Calculated Property
Pvap	994.24	kPa	397.19	Calculated Property
Pvap	1904.14	kPa	433.45	Calculated Property
Pvap	3305.79	kPa	469.70	Calculated Property
Pvap	[5.24e-05; 3383.57]	kPa	[143.42; 469.65]	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			8.19246e+01
Coefficient B			-5.77802e+03
Coefficient C			-1.04184e+01
Coefficient D			1.17821e-05
Coefficient E			0.00000e+00
Temperature range, min.			143.42
Temperature range, max.			469.65
Pvap	5.24e-05	kPa	143.42	Calculated Property
Pvap	0.02	kPa	179.67	Calculated Property
Pvap	0.75	kPa	215.92	Calculated Property
Pvap	8.55	kPa	252.16	Calculated Property
Pvap	47.31	kPa	288.41	Calculated Property
Pvap	167.67	kPa	324.66	Calculated Property
Pvap	445.64	kPa	360.91	Calculated Property
Pvap	979.81	kPa	397.15	Calculated Property
Pvap	1898.63	kPa	433.40	Calculated Property
Pvap	3383.57	kPa	469.65	Calculated Property
Pvap	[19.98; 269.99]	kPa	[268.80; 341.37]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.37906e+01
Coefficient B			-2.46519e+03
Coefficient C			-4.04540e+01
Reference			Osborn and Douslin, 1974
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			268.80
Temperature range, max.			341.37
Pvap	19.98	kPa	268.80	Calculated Property
Pvap	28.88	kPa	276.86	Calculated Property
Pvap	40.73	kPa	284.93	Calculated Property
Pvap	56.20	kPa	292.99	Calculated Property
Pvap	76.02	kPa	301.05	Calculated Property
Pvap	100.98	kPa	309.12	Calculated Property
Pvap	131.93	kPa	317.18	Calculated Property
Pvap	169.77	kPa	325.24	Calculated Property
Pvap	215.47	kPa	333.31	Calculated Property
Pvap	269.99	kPa	341.37	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[753.61; 246.84]	kg/m3	[143.42; 469.65]	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			5.58331e+01
Coefficient B			2.55740e-01
Coefficient C			4.69700e+02
Coefficient D			2.63190e-01
Temperature range, min.			143.42
Temperature range, max.			469.65
ρl	753.61	kg/m3	143.42	Calculated Property
ρl	725.65	kg/m3	179.67	Calculated Property
ρl	696.17	kg/m3	215.92	Calculated Property
ρl	664.81	kg/m3	252.16	Calculated Property
ρl	631.02	kg/m3	288.41	Calculated Property
ρl	593.96	kg/m3	324.66	Calculated Property
ρl	552.17	kg/m3	360.91	Calculated Property
ρl	502.70	kg/m3	397.15	Calculated Property
ρl	437.48	kg/m3	433.40	Calculated Property
ρl	246.84	kg/m3	469.65	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 0.01]	N/m	[143.45; 309.15]	Jasper (1972), surface tension of pure liquid compounds Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is γ in N/m, T in K
Coefficient A			4.88701e-02
Coefficient B			-1.12100e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			143.45
Temperature range, max.			309.15
γ	0.03	N/m	143.45	Calculated Property
γ	0.03	N/m	161.86	Calculated Property
γ	0.03	N/m	180.27	Calculated Property
γ	0.03	N/m	198.68	Calculated Property
γ	0.02	N/m	217.09	Calculated Property
γ	0.02	N/m	235.51	Calculated Property
γ	0.02	N/m	253.92	Calculated Property
γ	0.02	N/m	272.33	Calculated Property
γ	0.02	N/m	290.74	Calculated Property
γ	0.01	N/m	309.15	Calculated Property
γ	[0.03; 9.12e-04]	N/m	[143.42; 452.53]	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			-1.30120e-02
Coefficient B			1.77200e+01
Coefficient C			-3.03340e+00
Coefficient D			-2.87320e-04
Coefficient E			-5.61510e-06
Temperature range, min.			143.42
Temperature range, max.			452.53
γ	0.03	N/m	143.42	Calculated Property
γ	0.03	N/m	177.77	Calculated Property
γ	0.03	N/m	212.11	Calculated Property
γ	0.02	N/m	246.46	Calculated Property
γ	0.02	N/m	280.80	Calculated Property
γ	0.01	N/m	315.15	Calculated Property
γ	0.01	N/m	349.49	Calculated Property
γ	0.01	N/m	383.84	Calculated Property
γ	0.00	N/m	418.18	Calculated Property
γ	9.12e-04	N/m	452.53	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.00; 0.13]	W/m×K	[143.42; 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			-6.03200e+02
Coefficient B			7.46980e-01
Coefficient C			-8.18230e+08
Coefficient D			-8.78650e+09
Temperature range, min.			143.42
Temperature range, max.			1000.00
λgas	0.00	W/m×K	143.42	Calculated Property
λgas	0.01	W/m×K	238.60	Calculated Property
λgas	0.02	W/m×K	333.77	Calculated Property
λgas	0.03	W/m×K	428.95	Calculated Property
λgas	0.04	W/m×K	524.12	Calculated Property
λgas	0.05	W/m×K	619.30	Calculated Property
λgas	0.07	W/m×K	714.47	Calculated Property
λgas	0.09	W/m×K	809.65	Calculated Property
λgas	0.11	W/m×K	904.82	Calculated Property
λgas	0.13	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.17; 0.07]	W/m×K	[143.42; 445.00]	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			2.36490e-02
Coefficient B			-7.50890e+01
Coefficient C			-6.42290e-01
Coefficient D			-5.07800e-03
Coefficient E			-2.71960e-07
Temperature range, min.			143.42
Temperature range, max.			445.00
λliquid	0.17	W/m×K	143.42	Calculated Property
λliquid	0.16	W/m×K	176.93	Calculated Property
λliquid	0.15	W/m×K	210.44	Calculated Property
λliquid	0.13	W/m×K	243.95	Calculated Property
λliquid	0.12	W/m×K	277.46	Calculated Property
λliquid	0.11	W/m×K	310.96	Calculated Property
λliquid	0.09	W/m×K	344.47	Calculated Property
λliquid	0.08	W/m×K	377.98	Calculated Property
λliquid	0.08	W/m×K	411.49	Calculated Property
λliquid	0.07	W/m×K	445.00	Calculated Property

Similar Compounds

Find more compounds similar to Pentane.

Mixtures

• 1-Propanol + Pentane
• 1H-Imidazole, 1-methyl- + Pentane
• Benzene + Pentane
• Toluene + Pentane
• Benzene, (1-methylethyl)- + Pentane
• 1,1'-Biphenyl, 2-methyl- + Pentane
• n-Hexane + Pentane
• Heptane + Pentane
• Methane + Ethane + Pentane
• Pentane + Butane, 2-methyl-
• Methyl formate + Pentane
• Ethyl formate + Pentane
• Formic acid, propyl ester + Pentane
• Formic acid, butyl ester + Pentane
• Furfural + Pentane
• Pentane + N-Formylmorpholine
• 2-Pyrrolidinone, 1-methyl- + Pentane
• Benzene, 1,3-dimethyl- + Pentane
• Acetone + Pentane
• Pentane + Water

Find more mixtures with Pentane.

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).
• Hankinson and Thomson (1979), COSTALD parameters ChEDL chemicals 1.5.2, from Hankinson, R. W.; Thomson, G. H. A New Correlation for Saturated Densities of Liquids and Their Mixtures. AIChE J. 1979, 25, 653-663.
• IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 2 ChEDL chemicals 1.5.2, from Ambrose, D.; Tsonopoulos, C. Vapor-Liquid Critical Properties of Elements and Compounds. 2. Normal Alkanes. J. Chem. Eng. Data 1995, 40, 531-546.
• Jasper (1972), surface tension of pure liquid compounds ChEDL chemicals 1.5.2, from Jasper, J. J. The Surface Tension of Pure Liquid Compounds. J. Phys. Chem. Ref. Data 1972, 1, 841-1010 (as transcribed in Lange's Handbook).
• Passut and Danner (1973), critical constants and acentric factors ChEDL chemicals 1.5.2, from Passut, C. A.; Danner, R. P. Acentric Factor. A Valuable Correlating Parameter for the Properties of Hydrocarbons. Ind. Eng. Chem. Process Des. Dev. 1973, 12, 365-368.
• 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.
• Staveley, Lobo and Calado (1981), triple points ChEDL chemicals 1.5.2, from Staveley, L. A. K.; Lobo, L. Q.; Calado, J. C. G. Triple-Points of Low Melting Substances and Their Use in Cryogenic Work. Cryogenics 1981, 21, 131-144.
• 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.
• Thermal Diffusivity and Speed of Sound of Saturated Pentane from Light Scattering
• Determination of activity coefficients at infinite dilution of organic solutes in the ionic liquid, trihexyl(tetradecyl)-phosphonium tris(pentafluoroethyl) trifluorophosphate, by gas liquid chromatography
• Experimental liquid liquid equilibria of 1-methylimidazole with hydrocarbons and ethers
• Measurement and modeling of hydrocarbon dew points for five synthetic natural gas mixtures
• Determination of activity coefficients at infinite dilution of organic solutes in the ionic liquid, tributylmethylphosphonium methylsulphate by gas liquid chromatography
• Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent
• High-pressure vapor liquid equilibria in the nitrogen n-pentane system
• A simple apparatus for data solubility determination
• Thermal conductivity of polyurethane foam cell gases: Improved transient hot wire cell data of isopentane + n-pentane mixtures Extended Wassiljewa-model
• Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid N-butyl-4-methylpyridinium tosylate using GLC at T = (328.15, 333.15, 338.15, and 343.15)K
• Measurement and prediction of activity coefficients at infinite dilution ( ), vapor.liquid equilibria (VLE) and excess enthalpies (HE) of binary systems with 1,1-dialkyl-pyrrolidinium bis(trifluoromethylsulfonyl)imide using mod. UNIFAC (Dortmund)
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium trifluoromethanesulfonate using GLC
• Activity coefficients at infinite dilution measurements for organic solutes and water in the 1-hexyloxymethyl-3-methyl-imidazolium and 1,3-dihexyloxymethyl-imidazolium bis(trifluoromethylsulfonyl)-imide ionic liquids The cation influence
• Measurements of different thermodynamic properties of systems containing ionic liquids and correlation of these properties using modified UNIFAC (Dortmund)
• Gas-liquid chromatography measurements of activity coefficients at infinite dilution of hydrocarbons and alkanols in 1-alkyl-3-methylimidazolium bis(oxalato)borate
• Liquid liquid equilibria of imidazolium based ionic liquid + pyridine + hydrocarbon at 298.15 K: Experiments and correlations
• Validation of a new apparatus using the dynamic method for determining the critical properties of binary mixtures containing CO2 and a n-alkane
• Activity coefficients at infinite dilution of organic solutes in 1-octyl-3-methylimidazolium nitrate using gas-liquid chromatography
• Experimentation and thermodynamic representations of binaries containing compounds of low boiling points: Pentane and alkylmethanoates
• Study of critical and maximum temperatures of coexistence of liquid and gas phase in hydrocarbons binary mixtures of aromatic hydrocarbons with alkanes and cycloalkanes
• Phase equilibria measurements of ternary mixtures (sulfolane + a carboxylic acid + pentane) at 303.15 K
• Anomalous nucleation near a fluid phase boundary created by a rapid heat pulse
• Activity coefficients at infinite dilution of organic solvents and water in 1-butyl-3-methylimidazolium dicyanamide. A literature review of hexane/hex-1-ene separation
• High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
• Surface tension, density and composition in the methane-pentane system at high pressure
• Thermal conductivity of gaseous and liquid n-pentane
• Plotting of phase (vapor-liquid) transition surface near the critical point out of data from isochoric experiment. Experimental procedure
• New ionic liquid [P4,4,4,4][NTf2] in bio-butanol extraction on investigation of limiting activity coefficients
• Solubility of cinnamic acid in supercritical carbon dioxide and subcritical 1,1,1,2-tetrafluoroethane: Experimental data and modelling
• Measurements of activity coefficients at infinite dilution for organic solutes in two quaternary ammonium-based ionic liquids [DDA][ClO4] and [DDA][BF4]
• Application of trihexyltetradecylphosphonium dicyanamide ionic liquid for various types of separations problems: Activity coefficients at infinite dilution measurements utilizing GLC method
• The determination of activity coefficients at infinite dilution using g.l.c. for hydrocarbons in furfural at T = 278:15 K and T = 298:15 K
• Activity coefficients at infinite dilution for hydrocarbons in furfuryl alcohol at T=(278.15 and 298.15) K, determined by g.l.c.
• Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid 1-butyl-3-methyl-imidazolium 2-(2-methoxyethoxy) ethyl sulfate using g.l.c. at T = (298.15, 303.15, and 308.15) K
• Liquid phase behaviour of 1-hexyloxymethyl-3-methyl-imidazolium-based ionic liquids with hydrocarbons: The influence of anion
• Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid hexyl-3-methyl-imidazolium bis(trifluoromethylsulfonyl)-imide using g.l.c. at T = (298.15, 313.15, and 333.15) K
• Systems with ionic liquids: Measurement of VLE and c1 data and prediction of their thermodynamic behavior using original UNIFAC, mod. UNIFAC(Do) and COSMO-RS(Ol)
• Vapour pressures of n-pentane determined by comparative ebulliometry
• Experimental measurements and prediction of liquid densities for n-alkane mixtures
• Measurement of activity coefficients at infinite dilution using polar and non-polar solutes in the ionic liquid 1-methyl-3-octyl-imidazolium diethyleneglycolmonomethylethersulfate at T = (288.15, 298.15, and 313.15) K
• Excess molar volumes and dynamic viscosities for binary mixtures of toluene + n-alkanes (C5 C10) at T = 298.15 K Comparison with Prigogine Flory Patterson theory
• Thermodynamic study of (perfluoroalkane + alkane) mixtures: Excess and solvation enthalpies
• Development of a Henry s constant correlation and solubility measurements of n-pentane, i-pentane, cyclopentane, n-hexane, and toluene in water
• Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid trihexyltetradecylphosphonium-bis-(2,4,4-trimethylpentyl)- phosphinate using g.l.c. at T = (303.15, 308.15, 313.15, and 318.15) K
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid triethylsulphonium bis(trifluoromethylsulfonyl)imide
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 4-methyl-N-butyl-pyridinium bis(trifluoromethylsulfonyl)-imide
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium trifluoromethanesulfonate using gas liquid chromatography at T = (313.15, 323.15, and 333.15) K
• Experimental and theoretical study of surface tension of n-pentane, n-heptane, and some of their mixtures at different temperatures
• Activity coefficients at infinite dilution for solutes in the trioctylmethylammonium bis(trifluoromethylsulfonyl)imide ionic liquid 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
• Gas liquid chromatography measurements of activity coefficients at infinite dilution of various organic solutes and water in tri-iso-butylmethylphosphonium tosylate ionic liquid
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate [EMIM][TCB] using gas liquid chromatography
• Activity coefficients at infinite dilution of organic solutes in N-alkylpyridinium bis(trifluoromethylsulfonyl)imide ([CnPY][NTf2], n = 2, 4, 5) using gas liquid chromatography
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid trihexyl(tetradecyl)phosphonium tetrafluoroborate using gas liquid chromatography at T = (313.15, 333.15, 353.15, and 373.15) K
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-butyl-3-methylimidazolium hexafluoroantimonate using gas liquid chromatography at T = (313.15, 323.15, and 333.15) K
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid, methyl(trioctyl)ammonium thiosalicylate, [N1888][TS] by gas liquid chromatography at T = (303.15, 313.15, and 323.15) K
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(3-hydroxypropyl)pyridinium bis(trifluoromethylsulfonyl)-amide
• Thermodynamics and activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tetracyanoborate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-hexyl-3-methylimidazolium tetracyanoborate
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid trihexyltetradecylphosphonium hexafluorophosphate using gas liquid chromatography at T = (313.15, 333.15, 353.15, and 363.15) K
• Determination of infinite dilution activity coefficients using HS-SPME/GC/FID for hydrocarbons in furfural at temperatures of (298.15, 308.15, and 318.15) K
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpiperidinium bis(trifluoromethylsulfonyl)-amide
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpyrrolidinium bis(trifluoromethylsulfonyl)-amide
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium trifluorotris(perfluoroethyl)phosphate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpiperidinium trifluorotris(perfluoroethyl)phosphate
• Solubilities of evodiamine in twelve organic solvents from T = (283.2 to 323.2) K
• Experimental and theoretical study on infinite dilution activity coefficients of various solutes in piperidinium ionic liquids
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpyrrolidinium trifluorotris(perfluoroethyl)phosphate
• Activity coefficients at infinite dilution of organic solutes in N-formylmorpholine and N-methylpyrrolidone from gas-liquid chromatography
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-hydroxyethyl)- 3-methylimidazolium trifluorotris(perfluoroethyl)phosphate
• Activity coefficients at infinite dilution of organic solutes in diethylene glycol and triethylene glycol from gas-liquid chromatography
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid trihexyltetradecylphosphonium bis(trifluoromethylsulfonyl)imide using gas-liquid chromatography at T = (313.15, 333.15, 353.15 and 373.15) K
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tricyanomethanide
• Thermodynamics and activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylmorpholinium tricyanomethanide
• Measurement of activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium 2-(2-methoxyethoxy) ethylsulfate at T = (308.15, 313.15, 323.15 and 333.15) K using gas + liquid chromatography
• Measurement of activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-hexyl-1,4-diaza[2.2.2]bicyclooctanium bis(trifluoromethylsulfonyl)imide using gas-liquid chromatography
• Use of water in aiding olefin/paraffin (liquid + liquid) extraction via complexation with a silver bis(trifluoromethylsulfonyl)imide salt
• Activity coefficients at infinite dilution, physicochemical and thermodynamic properties for organic solutes and water in the ionic liquid ethyl-dimethyl-(2-methoxyethyl)ammonium trifluorotris-(perfluoroethyl)phosphate
• Activity coefficients at infinite dilution of alkanes, alkenes, alkyl benzenes in dimethylphosphate based ionic liquids using gas liquid chromatography
• Screening of environmental friendly ionic liquid as a solvent for the different types of separations problem: Insight from activity coefficients at infinite dilution measurement using (gas + liquid) chromatography technique
• A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
• Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-hexyl-2,3-dimethylimidazolium bis(trifluoromethylsulfonyl)imide
• Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
• Activity coefficients at infinite dilution of hydrocarbons in glycols: Experimental data and thermodynamic modeling with the GCA-EoS
• PVTx measurements and other derived volumetric properties of the binary ((1-propanol + n-pentane)) mixtures in the critical and supercritical regions
• Surface tension and density of mixtures of m-xylene + n-alkane at 293.15 K: Analysis under the extended Langmuir and Shereshefsky models
• Separation of water/butan-1-ol based on activity coefficients at infinite dilution in 1,3-didecyl-2-methylimidazolium dicyanamide ionic liquid
• Separation of binary mixtures based on gamma infinity data using [OMMIM][NTf2] ionic liquid and modelling of thermodynamic functions
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid trihexyl-tetradecyl-phosphonium tricyanomethanide
• Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in ionic liquid [HMMIM][BF4]
• Separation of binary mixtures based on gamma infinity data using [OMMIM][BF4] ionic liquid and modelling of thermodynamic functions
• Low cost apparatus for rapid boiling point determination of small air sensitive samples under inert atmosphere
• Isobaric specific heat capacities of emulsified kerosene at high temperature and pressure
• Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
• Solubility of Mercury in Liquid Hydrocarbons and Hydrocarbon Mixtures
• Isobaric Vapor Liquid Equilibrium for Nine Binary Systems of Cracking C5 Fraction at 250 kPa
• Simultaneous Measurement of Dynamic Viscosity and Density of n-Alkanes at High Pressures
• Isothermal Vapor-Liquid Equilibrium Data for Binary Mixtures of Hexafluoroethane (R116) + n-Pentane or n-Hexane at Two Temperatures, 288 and 296 K
• Experimental Phase Equilibrium for the Binary System of n-Pentane +2-Propanol Using a New Equilibrium Cell and the Static Total Pressure Method
• Determination of Activity Coefficients at Infinite Dilution of Organic Solutes in the Ionic Liquid 1-(2-Hydroxyethyl)-3-methylimidazolium Nonafluoro-1-butanesulfonate Using Gas-Liquid Chromatography
• Solubilities of Organic Semiconductors and Nonsteroidal Anti-inflammatory Drugs in Pure and Mixed Organic Solvents: Measurement and Modeling with Hansen Solubility Parameter
• Determination of Activity Coefficients at Infinite Dilution of Solutes in N,N'-Di(2-ethylhexyl)isobutyramide Using Inverse Gas-Liquid Chromatography
• Measurement and Prediction of Hydrocarbon Dew Points of Synthetic Natural Gas Mixtures
• Total Pressure Phase Equilibrium Measurements for the Binary Systems of n-Pentane + Cyclohexane and 1-Hexene + 2-Propanol
• Parametric Analysis of Mandelic Acid Separation from Aqueous Solutions by Using Secondary Amine Mixture (Amberlite LA-2) in Various Diluents
• Experimental High-Pressure Isochoric/Isoplethic Equilibrium for the Systems Propane + n-Pentane and Propane + Diethyl Ether
• Assessment of Pyrrolidinium-Based Ionic Liquid for the Separation of Binary Mixtures Based on Activity Coefficients at Infinite Dilution
• Liquid-Liquid Equilibrium Data for Ternary Systems Containing Alkanes (n-Pentane, n-Hexane, n-Heptane, and n-Octane) + Alcohol (Methanol and Ethanol) + Protic Ionic Liquid (2-HEAF)
• Thermodynamic Properties of Mixtures Containing Precursors of Vitamin B5
• Solubility of 1-Alkyl-3-methylimidazolium Hexafluorophosphate in Hydrocarbons
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Hexyl-3-methylimidazolium Hexafluorophosphate from Gas-Liquid Chromatography
• Determination of Activity Coefficients at Infinite Dilution of Solutes in the Ionic Liquid 1-Hexyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography at the Temperatures 298.15 K and 323.15 K
• Phase Behavior, Densities, and Isothermal Compressibility of CO2 + Pentane and CO2 + Acetone Systems in Various Phase Regions
• Phase Behavior, Densities and Isothermal Compressibility of CO2 + Pentane + Acetone Ternary System in Various Phase Regions
• Isothermal Vapor-Liquid Equilibria for the n-Pentane + 1-Butanol and n-Pentane + 2-Butanol Systems near the Critical Region of the Mixtures
• Determination of Activity Coefficients at Infinite Dilution of Solutes in the Ionic Liquid 1-Butyl-3-methylimidazolium Octyl Sulfate Using Gas-Liquid Chromatography at a Temperature of 298.15 K, 313.15 K, or 328.15 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
• 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
• Viscosities and Excess Molar Volumes of the Ternary System Toluene (1) + Cyclohexane (2) + Pentane (3) at 298.15 K
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 8. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 9. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in Trimethyl-butylammonium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography and Static Method
• Vapor-Liquid Equilibria for the n-Pentane + 1-Propanol and n-Pentane + 2-Methyl-1-propanol Systems near the Critical Region
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Infinite Dilution Activity Coefficients for Trihexyltetradecyl Phosphonium Ionic Liquids: Measurements and COSMO-RS Prediction
• Viscosities and Interfacial Properties of I-Methyl-3-butylimidazolium Hexafluorophosphate and 1-Isobutenyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
• Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Butyl-3-methyl-pyridinium Trifluoromethanesulfonate
• PVTx Measurements of Water-n-Pentane Mixtures in Critical and Supercritical Regions
• Activity Coefficients at Infinite Dilution for Hydrocarbons in Fatty Alcohols Determined by Gas-Liquid Chromatography
• Solubility of Benzoic Acid in Pure Solvents and Binary Mixtures
• Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Decyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Measurement and Correlation for the Solubilities of Dihydrocapsaicin in n-Heptane, n-Hexane, n-Pentane, Ethyl Acetate, Acetone, Ethanol, and Water
• Equilibrium Phase Densities, Interfacial Tensions for the Ethane + n-Pentane System at 294.15 K
• Vapor-Liquid Equilibria Measurements of the Methane + Pentane and Methane + Hexane Systems at Temperatures from (173 to 330) K and Pressures to 14 MPa
• Solubilities of 1-Hexyl-3-methylimidazole Nitrate and 1-Octyl-3-methylimidazole Nitrate in Selected Solvents
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Ethyl-3-methylimidazolium Diethylphosphate Using Gas Liquid Chromatography
• Equilibrium Phase Densities, Vapor Phase Compositions, and Interfacial Tensions for the Methane + Ethane + n-Pentane System at 294.15 K
• Apparent and Partial Molar Volumes at Infinite Dilution and Solid Liquid Equilibria of Dibenzothiophene + Alkane Systems
• Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
• Activity Coefficients at Infinite Dilution by GLC in Alkanediamines as Stationary Phases
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Dibutylphosphate Using Gas Liquid Chromatography
• Phase Equilibria of H2S-Hydrocarbons (Propane, n-Butane, and n-Pentane) Binary Systems at Low Temperatures
• Multiproperty Correlation of Experimental Data of the Binaries Propyl Ethanoate + Alkanes (Pentane to Decane). New Experimental Information for Vapor Liquid Equilibrium and Mixing Properties
• Solubilities of Rutaecarpine in Twelve Organic Solvents from (283.2 to 323.2) K
• Bubble-Point Measurements of Eight Binary Mixtures for Organic Rankine Cycle Applications
• Vapor Liquid Equilibrium for Several Compounds Relevant to the Biofuels Industry Modeled with the Wilson Equation
• Improvements in the Experimentation and the Representation of Thermodynamic Properties (iso-p VLE and yE) of Alkyl Propanoate + Alkane Binaries
• New Vapor Liquid Liquid Equilibrium Solubility Data for iso-Butane, n-Butane, n-Pentane, and n-Hexane in Alkanolamine Aqueous Solutions
• Enhancing liquid-phase olefin-paraffin separations using novel silver-based ionic liquids
• Liquid Liquid Equilibrium in Mixtures Containing Propane-1,2,3-triol and Mixtures Containing Vegetable Oils at Atmospheric Pressure
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Propyl-2,3-dimethylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Liquid - Liquid Equilibria for the Binary Systems of Sulfolane with Alkanes
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas-Liquid Chromatography
• Excess Enthalpies and Thermal Conductivity Coefficients for Binary Mixtures of Carbon Tetrachloride and Four Alkanes (C5 to C8) at a Temperature of 298.15 K
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Hexyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas-Liquid Chromatography
• Determination of Activity Coefficients at Infinite Dilution of Solutes in the Ionic Liquid, Trihexyltetradecylphosphonium Bis(trifluoromethylsulfonyl) Imide, Using Gas-Liquid Chromatography at T ) (303.15, 308.15, 313.15, and 318.15) K
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Ethyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Liquid-Liquid Equilibria in Ternary Systems 2-Methylbutane + 2-Methyl-2-propanol + Water and Pentane + 2-Methyl-2-propanol + Water at 293.15 K
• In Situ Determination of Phase Equilibria of Methyl Benzoate + Alkane Mixtures Using an Infrared Absorption Method. Comparison with Polar GC-SAFT Predictions
• Henry s Law Constants of Organic Compounds in Water and n-Octane at T = 293.2 K
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Ethyl-3-methylimidazolium Tris(pentafluoroethyl)trifluorophosphate [EMIM][FAP] Using Gas-Liquid Chromatography
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• NCMS SOLV-DB
• 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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