Chemical Properties of Cyclohexane (CAS 110-82-7)

InChI

InChI=1S/C6H12/c1-2-4-6-5-3-1/h1-6H2

InChI Key

XDTMQSROBMDMFD-UHFFFAOYSA-N

Formula

C6H12

SMILES

C1CCCCC1

Molecular Weight¹

84.16

CAS

110-82-7

Other Names

• Benzene, hexahydro-
• Cicloesano
• Cykloheksan
• Hexahydrobenzene
• Hexamethylene
• Hexanaphthene
• NSC 406835
• Rcra waste number U056
• UN 1145

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• T_ig : Autoignition Temperature (K).
• AP : Aniline Point (K).
• BasG : Gas basicity (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).
• LFL : Lower Flammability Limit (% in Air).
• UFL : Upper Flammability Limit (% in Air).
• 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.
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_c : Critical density (kg/m³).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• D^*_i : Self diffusion coefficient (m²/s).
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_gas : Molar entropy at standard conditions (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• c_sound,fluid : Speed of sound in fluid (m/s).
• γ : Surface Tension (N/m).
• Δ_vapS : Entropy of vaporization at a given temperature (J/mol×K).
• T_boil : Normal Boiling Point Temperature (K).
• T_boil : Boiling point at given pressure (K).
• T_c : Critical Temperature (K).
• λ : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• V_c : Critical Volume (m³/kmol).
• V_m : Molar Volume (m³/mol).
• 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	0.2120		KDB
PAff	686.90	kJ/mol	NIST
Tig	543.15	K	KDB
AP	304.150	K	KDB
BasG	666.90	kJ/mol	NIST
ΔcH°liquid	[-3947.00; -3918.00]	kJ/mol
ΔcH°liquid	-3918.60 ± 0.70	kJ/mol	NIST
ΔcH°liquid	-3918.40 ± 1.00	kJ/mol	NIST
ΔcH°liquid	-3919.90 ± 0.71	kJ/mol	NIST
ΔcH°liquid	-3919.60 ± 1.30	kJ/mol	NIST
ΔcH°liquid	-3918.00 ± 0.75	kJ/mol	NIST
ΔcH°liquid	-3935.30	kJ/mol	NIST
ΔcH°liquid	Outlier -3947.00	kJ/mol	NIST
μ	0.30	debye	KDB
η	0.0008920	Pa×s	Densiti...
LFL	1.33	% in Air	KDB
UFL	8.35	% in Air	KDB
Tflash,oc	253.15	K	KDB
ΔfG°	31.78	kJ/mol	KDB
Rg	3.2610		KDB
Δc,grossH	3919.82	kJ/mol	KDB
Δc,netH	3655.770	kJ/mol	KDB
ΔfH°gas	[-124.60; -123.10]	kJ/mol
ΔfH°gas	-123.20	kJ/mol	KDB
ΔfH°gas	-124.60	kJ/mol	NIST
ΔfH°gas	-123.10 ± 0.79	kJ/mol	NIST
ΔfH°gas	-123.30	kJ/mol	NIST
ΔfH°liquid	[-157.70; -156.20]	kJ/mol
ΔfH°liquid	-157.70 ± 1.80	kJ/mol	NIST
ΔfH°liquid	-156.20 ± 0.79	kJ/mol	NIST
ΔfH°liquid	-156.40 ± 1.30	kJ/mol	NIST
ΔfusH°	2.06	kJ/mol	Joback Calculated Property
ΔvapH°	[30.10; 33.50]	kJ/mol
ΔvapH°	33.12	kJ/mol	NIST
ΔvapH°	33.10	kJ/mol	NIST
ΔvapH°	33.00 ± 0.10	kJ/mol	NIST
ΔvapH°	32.79 ± 0.14	kJ/mol	NIST
ΔvapH°	33.00	kJ/mol	NIST
ΔvapH°	33.00 ± 0.10	kJ/mol	NIST
ΔvapH°	33.00	kJ/mol	NIST
ΔvapH°	32.90 ± 0.30	kJ/mol	NIST
ΔvapH°	32.90	kJ/mol	NIST
ΔvapH°	33.00 ± 0.02	kJ/mol	NIST
ΔvapH°	33.00 ± 0.10	kJ/mol	NIST
ΔvapH°	Outlier 30.10	kJ/mol	NIST
ΔvapH°	33.04	kJ/mol	NIST
ΔvapH°	33.50	kJ/mol	NIST
ΔvapH°	33.00	kJ/mol	NIST
ΔvapH°	33.03	kJ/mol	NIST
ΔvapH°	33.00	kJ/mol	NIST
ΔvapH°	33.10	kJ/mol	NIST
ΔvapH°	33.30 ± 0.10	kJ/mol	NIST
ΔvapH°	33.50	kJ/mol	NIST
ΔvapH°	Outlier 30.20 ± 0.30	kJ/mol	NIST
IE	[9.79; 11.00]	eV
IE	9.88 ± 0.03	eV	NIST
IE	9.80 ± 0.05	eV	NIST
IE	10.00 ± 0.03	eV	NIST
IE	9.82	eV	NIST
IE	9.88 ± 0.10	eV	NIST
IE	9.88	eV	NIST
IE	9.88 ± 0.02	eV	NIST
IE	9.88	eV	NIST
IE	9.89 ± 0.01	eV	NIST
IE	9.83 ± 0.05	eV	NIST
IE	9.84	eV	NIST
IE	9.88 ± 0.01	eV	NIST
IE	9.87	eV	NIST
IE	9.88 ± 0.01	eV	NIST
IE	9.89	eV	NIST
IE	9.81	eV	NIST
IE	9.79	eV	NIST
IE	9.88 ± 0.02	eV	NIST
IE	Outlier 11.00 ± 0.20	eV	NIST
IE	10.32	eV	NIST
IE	10.30 ± 0.10	eV	NIST
IE	10.30	eV	NIST
log10WS	[-3.10; -3.10]
log10WS	-3.10		Aq. Sol...
log10WS	-3.10		Estimat...
logPoct/wat	2.341		Crippen Calculated Property
McVol	84.540	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
NFPA Health	1		KDB
Pc	[4033.30; 4200.00]	kPa
Pc	4080.00	kPa	KDB
Pc	4060.00	kPa	Critica...
Pc	Outlier 4200.00	kPa	Critica...
Pc	4080.00 ± 30.00	kPa	NIST
Pc	4071.00 ± 20.00	kPa	NIST
Pc	4075.00 ± 2.00	kPa	NIST
Pc	4097.00 ± 10.34	kPa	NIST
Pc	4036.00 ± 60.00	kPa	NIST
Pc	4110.76 ± 101.32	kPa	NIST
Pc	4036.70 ± 39.99	kPa	NIST
Pc	4033.30 ± 10.67	kPa	NIST
Ptriple	5.40	kPa	KDB
ρc	[271.84; 274.36]	kg/m3
ρc	272.68 ± 2.52	kg/m3	NIST
ρc	274.36 ± 5.89	kg/m3	NIST
ρc	271.84 ± 3.37	kg/m3	NIST
ρc	273.52 ± 1.68	kg/m3	NIST
ρc	273.27 ± 5.05	kg/m3	NIST
Inp	[619.00; 700.00]
Inp	664.10		NIST
Inp	660.10		NIST
Inp	665.70		NIST
Inp	662.30		NIST
Inp	661.20		NIST
Inp	661.90		NIST
Inp	662.90		NIST
Inp	681.00		NIST
Inp	676.00		NIST
Inp	667.14		NIST
Inp	667.02		NIST
Inp	667.46		NIST
Inp	656.80		NIST
Inp	662.20		NIST
Inp	Outlier 693.60		NIST
Inp	663.35		NIST
Inp	668.00		NIST
Inp	649.00		NIST
Inp	650.00		NIST
Inp	672.00		NIST
Inp	Outlier 688.30		NIST
Inp	Outlier 697.90		NIST
Inp	658.00		NIST
Inp	655.70		NIST
Inp	Outlier 692.80		NIST
Inp	649.00		NIST
Inp	Outlier 694.00		NIST
Inp	660.60		NIST
Inp	665.60		NIST
Inp	660.60		NIST
Inp	665.60		NIST
Inp	662.70		NIST
Inp	667.10		NIST
Inp	663.00		NIST
Inp	664.00		NIST
Inp	658.00		NIST
Inp	663.00		NIST
Inp	668.00		NIST
Inp	676.00		NIST
Inp	662.00		NIST
Inp	666.40		NIST
Inp	671.10		NIST
Inp	674.00		NIST
Inp	680.00		NIST
Inp	669.00		NIST
Inp	658.70		NIST
Inp	660.90		NIST
Inp	663.20		NIST
Inp	665.50		NIST
Inp	680.00		NIST
Inp	673.60		NIST
Inp	658.00		NIST
Inp	685.00		NIST
Inp	656.00		NIST
Inp	658.00		NIST
Inp	660.00		NIST
Inp	663.00		NIST
Inp	665.00		NIST
Inp	668.00		NIST
Inp	664.50		NIST
Inp	666.80		NIST
Inp	669.20		NIST
Inp	671.70		NIST
Inp	674.40		NIST
Inp	677.30		NIST
Inp	663.70		NIST
Inp	664.20		NIST
Inp	675.00		NIST
Inp	661.00		NIST
Inp	683.00		NIST
Inp	669.00		NIST
Inp	Outlier 639.00		NIST
Inp	680.00		NIST
Inp	661.00		NIST
Inp	661.00		NIST
Inp	662.00		NIST
Inp	661.00		NIST
Inp	661.00		NIST
Inp	657.20		NIST
Inp	659.60		NIST
Inp	662.10		NIST
Inp	664.70		NIST
Inp	667.40		NIST
Inp	670.30		NIST
Inp	657.00		NIST
Inp	659.10		NIST
Inp	661.30		NIST
Inp	663.60		NIST
Inp	666.10		NIST
Inp	668.80		NIST
Inp	662.00		NIST
Inp	663.00		NIST
Inp	669.20		NIST
Inp	668.10		NIST
Inp	Outlier 690.00		NIST
Inp	675.00		NIST
Inp	662.70		NIST
Inp	663.90		NIST
Inp	662.78		NIST
Inp	674.00		NIST
Inp	664.00		NIST
Inp	668.80		NIST
Inp	667.80		NIST
Inp	675.60		NIST
Inp	671.00		NIST
Inp	660.00		NIST
Inp	668.00		NIST
Inp	663.00		NIST
Inp	668.00		NIST
Inp	674.00		NIST
Inp	663.00		NIST
Inp	667.00		NIST
Inp	674.00		NIST
Inp	Outlier 689.00		NIST
Inp	669.00		NIST
Inp	662.00		NIST
Inp	662.00		NIST
Inp	664.00		NIST
Inp	675.70		NIST
Inp	682.00		NIST
Inp	674.00		NIST
Inp	683.00		NIST
Inp	662.00		NIST
Inp	665.00		NIST
Inp	667.00		NIST
Inp	669.00		NIST
Inp	672.00		NIST
Inp	663.80		NIST
Inp	667.00		NIST
Inp	674.00		NIST
Inp	662.00		NIST
Inp	Outlier 700.00		NIST
Inp	667.00		NIST
Inp	667.00		NIST
Inp	667.00		NIST
Inp	676.00		NIST
Inp	667.00		NIST
Inp	Outlier 688.00		NIST
Inp	658.00		NIST
Inp	664.00		NIST
Inp	668.00		NIST
Inp	672.00		NIST
Inp	656.00		NIST
Inp	658.00		NIST
Inp	660.00		NIST
Inp	664.00		NIST
Inp	667.00		NIST
Inp	675.00		NIST
Inp	675.00		NIST
Inp	Outlier 689.00		NIST
Inp	675.00		NIST
Inp	668.00		NIST
Inp	668.00		NIST
Inp	676.00		NIST
Inp	Outlier 688.00		NIST
Inp	676.00		NIST
Inp	650.00		NIST
Inp	678.00		NIST
Inp	657.80		NIST
Inp	658.00		NIST
Inp	663.00		NIST
Inp	655.80		NIST
Inp	647.56		NIST
Inp	648.22		NIST
Inp	656.20		NIST
Inp	654.90		NIST
Inp	655.40		NIST
Inp	656.20		NIST
Inp	657.60		NIST
Inp	654.60		NIST
Inp	655.40		NIST
Inp	656.20		NIST
Inp	657.60		NIST
Inp	656.20		NIST
Inp	654.90		NIST
Inp	651.20		NIST
Inp	651.24		NIST
Inp	651.00		NIST
Inp	651.09		NIST
Inp	651.14		NIST
Inp	651.00		NIST
Inp	668.00		NIST
Inp	660.80		NIST
Inp	657.30		NIST
Inp	656.40		NIST
Inp	647.36		NIST
Inp	650.41		NIST
Inp	652.19		NIST
Inp	653.15		NIST
Inp	656.24		NIST
Inp	658.10		NIST
Inp	662.00		NIST
Inp	650.00		NIST
Inp	665.00		NIST
Inp	648.90		NIST
Inp	662.00		NIST
Inp	662.00		NIST
Inp	673.00		NIST
Inp	680.00		NIST
Inp	685.00		NIST
Inp	668.00		NIST
Inp	660.00		NIST
Inp	663.00		NIST
Inp	661.00		NIST
Inp	665.00		NIST
Inp	Outlier 619.00		NIST
Inp	Outlier 625.00		NIST
Inp	661.00		NIST
Inp	Outlier 688.00		NIST
Inp	676.00		NIST
Inp	658.00		NIST
Inp	651.00		NIST
Inp	666.00		NIST
Inp	662.00		NIST
Inp	654.90		NIST
Inp	648.95		NIST
Inp	658.00		NIST
Inp	670.00		NIST
Inp	658.00		NIST
Inp	651.00		NIST
Inp	668.00		NIST
Inp	659.00		NIST
Inp	660.00		NIST
Inp	669.00		NIST
Inp	669.00		NIST
Inp	663.00		NIST
Inp	661.00		NIST
Inp	677.00		NIST
Inp	657.00		NIST
Inp	Outlier 696.00		NIST
Inp	Outlier 700.00		NIST
Inp	664.00		NIST
Inp	666.00		NIST
Inp	657.00		NIST
Inp	666.00		NIST
Inp	666.00		NIST
Inp	654.00		NIST
Inp	649.00		NIST
Inp	649.00		NIST
Inp	664.00		NIST
Inp	650.00		NIST
Inp	666.00		NIST
Inp	664.00		NIST
Inp	677.00		NIST
Inp	666.00		NIST
Inp	645.00		NIST
Inp	661.00		NIST
Inp	669.00		NIST
Inp	675.00		NIST
Inp	664.00		NIST
Inp	675.00		NIST
Inp	669.00		NIST
Inp	675.00		NIST
Inp	669.00		NIST
Inp	658.00		NIST
Inp	648.95		NIST
Inp	668.00		NIST
Inp	663.00		NIST
Inp	654.90		NIST
Inp	655.40		NIST
Inp	651.20		NIST
Inp	651.00		NIST
Inp	647.36		NIST
Inp	658.10		NIST
Inp	650.00		NIST
Inp	665.00		NIST
I	[712.00; 766.00]
I	740.00		NIST
I	766.00		NIST
I	748.00		NIST
I	752.00		NIST
I	757.00		NIST
I	740.00		NIST
I	735.00		NIST
I	742.00		NIST
I	766.00		NIST
I	726.00		NIST
I	732.00		NIST
I	738.00		NIST
I	752.00		NIST
I	722.00		NIST
I	722.00		NIST
I	722.00		NIST
I	732.00		NIST
I	734.00		NIST
I	735.50		NIST
I	737.00		NIST
I	741.70		NIST
I	723.00		NIST
I	729.00		NIST
I	729.00		NIST
I	717.00		NIST
I	712.00		NIST
I	765.00		NIST
I	742.00		NIST
I	737.00		NIST
I	765.00		NIST
I	723.00		NIST
I	756.00		NIST
I	723.00		NIST
I	726.00		NIST
I	722.00		NIST
S°gas	298.19	J/mol×K	NIST
S°liquid	[203.89; 205.90]	J/mol×K
S°liquid	203.89	J/mol×K	NIST
S°liquid	204.35	J/mol×K	NIST
S°liquid	205.90	J/mol×K	NIST
Tboil	[342.10; 358.70]	K
Tboil	353.88	K	KDB
Tboil	353.73	K	Isobari...
Tboil	353.73	K	Isobari...
Tboil	353.70	K	Isobari...
Tboil	353.78	K	A novel...
Tboil	355.00	K	The rol...
Tboil	353.70	K	Excess ...
Tboil	353.94	K	Isobari...
Tboil	353.95	K	Excess ...
Tboil	353.82	K	A new a...
Tboil	353.85	K	Vapor L...
Tboil	353.82	K	A New T...
Tboil	353.78	K	Vapor-L...
Tboil	353.73	K	Isobari...
Tboil	353.73	K	Isobari...
Tboil	353.90	K	Isobari...
Tboil	353.93 ± 0.10	K	NIST
Tboil	353.84 ± 0.10	K	NIST
Tboil	353.85 ± 0.20	K	NIST
Tboil	353.95 ± 0.10	K	NIST
Tboil	353.88 ± 0.20	K	NIST
Tboil	353.81 ± 0.15	K	NIST
Tboil	354.00 ± 1.00	K	NIST
Tboil	354.15 ± 0.30	K	NIST
Tboil	353.90 ± 0.08	K	NIST
Tboil	353.70 ± 0.30	K	NIST
Tboil	353.90	K	NIST
Tboil	353.25 ± 0.30	K	NIST
Tboil	353.25 ± 0.50	K	NIST
Tboil	353.25 ± 0.50	K	NIST
Tboil	353.88 ± 0.10	K	NIST
Tboil	353.90	K	NIST
Tboil	354.60 ± 0.30	K	NIST
Tboil	353.95 ± 0.20	K	NIST
Tboil	353.90 ± 0.40	K	NIST
Tboil	353.84 ± 0.20	K	NIST
Tboil	353.85 ± 0.30	K	NIST
Tboil	353.25 ± 0.15	K	NIST
Tboil	354.00 ± 0.40	K	NIST
Tboil	353.90 ± 0.30	K	NIST
Tboil	353.25 ± 0.30	K	NIST
Tboil	354.00 ± 0.30	K	NIST
Tboil	353.95 ± 0.20	K	NIST
Tboil	353.91 ± 0.15	K	NIST
Tboil	353.85 ± 0.20	K	NIST
Tboil	353.95 ± 0.50	K	NIST
Tboil	353.40 ± 0.50	K	NIST
Tboil	353.90 ± 0.40	K	NIST
Tboil	353.85 ± 0.30	K	NIST
Tboil	353.87 ± 0.01	K	NIST
Tboil	353.70 ± 0.10	K	NIST
Tboil	353.85 ± 0.30	K	NIST
Tboil	353.87 ± 0.20	K	NIST
Tboil	353.89 ± 0.20	K	NIST
Tboil	354.00 ± 0.20	K	NIST
Tboil	353.70 ± 1.00	K	NIST
Tboil	353.88 ± 0.20	K	NIST
Tboil	353.89 ± 0.15	K	NIST
Tboil	353.85 ± 0.20	K	NIST
Tboil	354.15 ± 1.50	K	NIST
Tboil	353.85 ± 0.20	K	NIST
Tboil	353.85 ± 0.30	K	NIST
Tboil	353.85 ± 0.30	K	NIST
Tboil	353.85 ± 0.30	K	NIST
Tboil	353.93 ± 0.30	K	NIST
Tboil	353.55 ± 0.30	K	NIST
Tboil	353.95 ± 0.50	K	NIST
Tboil	353.89 ± 0.40	K	NIST
Tboil	353.70 ± 2.00	K	NIST
Tboil	353.90 ± 0.30	K	NIST
Tboil	353.90 ± 0.50	K	NIST
Tboil	353.90 ± 0.50	K	NIST
Tboil	353.72 ± 0.30	K	NIST
Tboil	354.08 ± 0.20	K	NIST
Tboil	354.15 ± 0.40	K	NIST
Tboil	353.95 ± 0.25	K	NIST
Tboil	353.90 ± 0.50	K	NIST
Tboil	354.00 ± 0.30	K	NIST
Tboil	353.00 ± 3.00	K	NIST
Tboil	353.89 ± 0.15	K	NIST
Tboil	353.80 ± 0.50	K	NIST
Tboil	353.15 ± 1.00	K	NIST
Tboil	353.95 ± 0.30	K	NIST
Tboil	353.81 ± 0.20	K	NIST
Tboil	352.35 ± 1.50	K	NIST
Tboil	353.80 ± 0.50	K	NIST
Tboil	353.80 ± 0.30	K	NIST
Tboil	353.87 ± 0.15	K	NIST
Tboil	354.00 ± 0.30	K	NIST
Tboil	354.00 ± 0.50	K	NIST
Tboil	353.95 ± 0.30	K	NIST
Tboil	353.90 ± 0.30	K	NIST
Tboil	353.80 ± 0.50	K	NIST
Tboil	353.88 ± 0.01	K	NIST
Tboil	353.90 ± 1.00	K	NIST
Tboil	353.70 ± 1.00	K	NIST
Tboil	354.10 ± 0.40	K	NIST
Tboil	353.15 ± 0.50	K	NIST
Tboil	353.89 ± 0.05	K	NIST
Tboil	353.95 ± 0.30	K	NIST
Tboil	353.89 ± 0.10	K	NIST
Tboil	353.75 ± 0.40	K	NIST
Tboil	353.96 ± 0.10	K	NIST
Tboil	353.95 ± 0.20	K	NIST
Tboil	354.10 ± 0.60	K	NIST
Tboil	354.05 ± 0.40	K	NIST
Tboil	353.95 ± 0.20	K	NIST
Tboil	354.40 ± 1.00	K	NIST
Tboil	353.00 ± 3.00	K	NIST
Tboil	354.05 ± 0.30	K	NIST
Tboil	353.95 ± 0.40	K	NIST
Tboil	354.07 ± 0.30	K	NIST
Tboil	354.15 ± 1.50	K	NIST
Tboil	353.65 ± 0.60	K	NIST
Tboil	353.90 ± 0.30	K	NIST
Tboil	353.90 ± 0.50	K	NIST
Tboil	354.15 ± 0.30	K	NIST
Tboil	353.95 ± 0.10	K	NIST
Tboil	353.87 ± 0.10	K	NIST
Tboil	354.00 ± 1.00	K	NIST
Tboil	354.55 ± 0.30	K	NIST
Tboil	354.00 ± 0.50	K	NIST
Tboil	354.55 ± 0.20	K	NIST
Tboil	356.40 ± 2.00	K	NIST
Tboil	Outlier 356.65 ± 0.50	K	NIST
Tboil	Outlier 342.10 ± 0.20	K	NIST
Tboil	353.00 ± 2.00	K	NIST
Tboil	355.00 ± 3.00	K	NIST
Tboil	354.00 ± 2.00	K	NIST
Tboil	354.00 ± 1.50	K	NIST
Tboil	Outlier 345.20 ± 8.00	K	NIST
Tboil	Outlier 358.70 ± 3.33	K	NIST
Tc	[552.97; 555.10]	K
Tc	553.80	K	KDB
Tc	553.60	K	Measure...
Tc	554.10	K	Measure...
Tc	553.61	K	Experim...
Tc	553.60	K	Gas-Liq...
Tc	553.80 ± 0.20	K	NIST
Tc	553.90 ± 0.40	K	NIST
Tc	553.70 ± 0.60	K	NIST
Tc	553.40	K	NIST
Tc	553.64 ± 0.03	K	NIST
Tc	553.00 ± 0.30	K	NIST
Tc	Outlier 555.10 ± 0.50	K	NIST
Tc	553.40 ± 0.60	K	NIST
Tc	553.35 ± 0.10	K	NIST
Tc	553.40 ± 0.60	K	NIST
Tc	553.45 ± 0.15	K	NIST
Tc	554.15 ± 1.50	K	NIST
Tc	553.40 ± 0.60	K	NIST
Tc	552.97 ± 0.10	K	NIST
Tc	553.90 ± 0.20	K	NIST
Tc	554.20 ± 1.00	K	NIST
Tc	553.00 ± 2.00	K	NIST
Tc	553.20 ± 0.60	K	NIST
Tfus	[266.75; 280.69]	K
Tfus	279.96	K	Aq. Sol...
Tfus	279.70	K	KDB
Tfus	280.10	K	Phase d...
Tfus	280.00	K	Determi...
Tfus	279.95	K	Liquid-...
Tfus	279.96	K	Solid-L...
Tfus	280.15 ± 1.00	K	NIST
Tfus	279.74 ± 0.02	K	NIST
Tfus	279.66 ± 0.10	K	NIST
Tfus	279.74 ± 0.08	K	NIST
Tfus	279.73 ± 0.01	K	NIST
Tfus	279.87 ± 0.01	K	NIST
Tfus	279.70 ± 0.05	K	NIST
Tfus	280.69 ± 0.05	K	NIST
Tfus	279.73 ± 0.15	K	NIST
Tfus	279.72 ± 0.04	K	NIST
Tfus	279.70 ± 0.03	K	NIST
Tfus	279.58 ± 0.10	K	NIST
Tfus	279.75 ± 0.30	K	NIST
Tfus	279.69 ± 0.10	K	NIST
Tfus	279.22 ± 0.10	K	NIST
Tfus	279.70 ± 0.20	K	NIST
Tfus	279.70 ± 0.30	K	NIST
Tfus	279.65 ± 0.10	K	NIST
Tfus	279.65 ± 0.30	K	NIST
Tfus	279.62 ± 0.20	K	NIST
Tfus	279.55 ± 0.20	K	NIST
Tfus	279.57 ± 0.06	K	NIST
Tfus	279.50 ± 0.07	K	NIST
Tfus	279.69 ± 0.01	K	NIST
Tfus	279.30 ± 0.80	K	NIST
Tfus	279.51 ± 0.06	K	NIST
Tfus	279.65 ± 0.10	K	NIST
Tfus	279.55 ± 0.20	K	NIST
Tfus	279.55 ± 0.50	K	NIST
Tfus	279.55 ± 0.20	K	NIST
Tfus	Outlier 266.75 ± 1.50	K	NIST
Tfus	277.15 ± 1.00	K	NIST
Tfus	279.55 ± 0.10	K	NIST
Tfus	279.00 ± 1.50	K	NIST
Tfus	279.40 ± 1.00	K	NIST
Tfus	279.15 ± 0.50	K	NIST
Tfus	279.35 ± 0.50	K	NIST
Tfus	279.40 ± 0.60	K	NIST
Tfus	279.55 ± 0.20	K	NIST
Tfus	277.70 ± 1.00	K	NIST
Tfus	279.55 ± 0.40	K	NIST
Tfus	279.55 ± 0.20	K	NIST
Tfus	278.65 ± 0.20	K	NIST
Tfus	279.65 ± 0.50	K	NIST
Tfus	279.60 ± 2.00	K	NIST
Tfus	277.90 ± 0.60	K	NIST
Tfus	278.70 ± 2.77	K	NIST
Ttriple	[186.18; 279.90]	K
Ttriple	279.83	K	KDB
Ttriple	Outlier 186.18	K	Develop...
Ttriple	279.70 ± 0.10	K	NIST
Ttriple	279.83 ± 0.02	K	NIST
Ttriple	279.90 ± 3.00	K	NIST
Ttriple	279.84 ± 0.02	K	NIST
Ttriple	279.82 ± 0.05	K	NIST
Ttriple	279.40 ± 0.20	K	NIST
Ttriple	279.78 ± 0.06	K	NIST
Ttriple	279.30 ± 0.20	K	NIST
Vc	[0.308; 0.309]	m3/kmol
Vc	0.308	m3/kmol	KDB
Vc	0.308	m3/kmol	NIST
Vc	0.309 ± 0.003	m3/kmol	NIST
Vm	[1.09e-04; 1.09e-04]	m3/mol
Vm	1.09e-04	m3/mol	Excess ...
Vm	1.09e-04	m3/mol	Thermod...
Vm	1.09e-04	m3/mol	Excess ...
Zc	0.2729110		KDB
Zra	0.27		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[138.07; 206.30]	J/mol×K	[370.00; 544.00]
Cp,gas	138.07	J/mol×K	370.00	NIST
Cp,gas	143.10 ± 1.30	J/mol×K	384.00	NIST
Cp,gas	146.44	J/mol×K	390.00	NIST
Cp,gas	153.97	J/mol×K	410.00	NIST
Cp,gas	161.80 ± 1.70	J/mol×K	428.00	NIST
Cp,gas	174.50 ± 1.70	J/mol×K	460.00	NIST
Cp,gas	189.50 ± 2.10	J/mol×K	495.00	NIST
Cp,gas	196.70 ± 2.10	J/mol×K	521.00	NIST
Cp,gas	206.30 ± 2.10	J/mol×K	544.00	NIST
Cp,liquid	[100.40; 176.10]	J/mol×K	[293.15; 326.50]
Cp,liquid	154.81	J/mol×K	293.15	NIST
Cp,liquid	153.75	J/mol×K	293.15	Excess ...
Cp,liquid	155.13	J/mol×K	293.15	NIST
Cp,liquid	154.80	J/mol×K	293.15	NIST
Cp,liquid	155.85	J/mol×K	295.00	NIST
Cp,liquid	152.93	J/mol×K	298.00	NIST
Cp,liquid	155.50	J/mol×K	298.00	NIST
Cp,liquid	156.70	J/mol×K	298.00	NIST
Cp,liquid	155.31	J/mol×K	298.00	NIST
Cp,liquid	176.10	J/mol×K	298.00	NIST
Cp,liquid	156.20	J/mol×K	298.15	Excess ...
Cp,liquid	156.50	J/mol×K	298.15	NIST
Cp,liquid	155.96	J/mol×K	298.15	NIST
Cp,liquid	157.06	J/mol×K	298.15	NIST
Cp,liquid	156.40	J/mol×K	298.15	NIST
Cp,liquid	156.00	J/mol×K	298.15	NIST
Cp,liquid	156.15	J/mol×K	298.15	NIST
Cp,liquid	156.12	J/mol×K	298.15	NIST
Cp,liquid	156.40	J/mol×K	298.15	NIST
Cp,liquid	154.32	J/mol×K	298.15	NIST
Cp,liquid	155.96	J/mol×K	298.15	NIST
Cp,liquid	156.12	J/mol×K	298.15	NIST
Cp,liquid	156.07	J/mol×K	298.15	NIST
Cp,liquid	156.07	J/mol×K	298.15	NIST
Cp,liquid	156.20	J/mol×K	298.15	NIST
Cp,liquid	156.31	J/mol×K	298.15	NIST
Cp,liquid	159.60	J/mol×K	298.15	NIST
Cp,liquid	155.20	J/mol×K	298.15	NIST
Cp,liquid	156.90	J/mol×K	298.15	NIST
Cp,liquid	156.00	J/mol×K	298.15	NIST
Cp,liquid	155.85	J/mol×K	298.15	NIST
Cp,liquid	156.35	J/mol×K	298.15	NIST
Cp,liquid	143.90	J/mol×K	298.90	NIST
Cp,liquid	154.20	J/mol×K	300.00	NIST
Cp,liquid	158.95	J/mol×K	303.15	Excess ...
Cp,liquid	100.40	J/mol×K	304.20	NIST
Cp,liquid	155.20	J/mol×K	311.00	NIST
Cp,liquid	143.90	J/mol×K	326.50	NIST
η	[0.0005195; 0.0011802]	Pa×s	[283.15; 333.15]
η	0.0011802	Pa×s	283.15	Density...
η	0.0010770	Pa×s	288.15	Densiti...
η	0.0009840	Pa×s	293.15	Densiti...
η	0.0009847	Pa×s	293.15	Density...
η	0.0009680	Pa×s	293.15	Dynamic...
η	0.0009840	Pa×s	293.15	Densiti...
η	0.0009680	Pa×s	293.15	Dynamic...
η	0.0009680	Pa×s	293.15	Viscosi...
η	0.0009027	Pa×s	298.15	Thermod...
η	0.0009040	Pa×s	298.15	Densiti...
η	0.0008870	Pa×s	298.15	Dynamic...
η	0.0008980	Pa×s	298.15	Densiti...
η	0.0009030	Pa×s	298.15	Densiti...
η	0.0008945	Pa×s	298.15	Thermop...
η	0.0008870	Pa×s	298.15	Dynamic...
η	0.0009030	Pa×s	298.15	Densiti...
η	0.0008870	Pa×s	298.15	Viscosi...
η	0.0008205	Pa×s	303.15	Thermod...
η	0.0008300	Pa×s	303.15	Densiti...
η	0.0008284	Pa×s	303.15	Thermop...
η	0.0008300	Pa×s	303.15	Densiti...
η	0.0008090	Pa×s	303.15	Densiti...
η	0.0008160	Pa×s	303.15	Dynamic...
η	0.0008160	Pa×s	303.15	Dynamic...
η	0.0008230	Pa×s	303.15	Density...
η	0.0008160	Pa×s	303.15	Viscosi...
η	0.0008210	Pa×s	303.15	Thermod...
η	0.0008295	Pa×s	303.15	Density...
η	0.0007490	Pa×s	308.15	Densiti...
η	0.0007720	Pa×s	308.15	Density...
η	0.0007637	Pa×s	308.15	Thermop...
η	0.0007640	Pa×s	308.15	Densiti...
η	0.0006850	Pa×s	313.15	Density...
η	0.0007061	Pa×s	313.15	Density...
η	0.0006960	Pa×s	313.15	Thermod...
η	0.0006963	Pa×s	313.15	Thermod...
η	0.0006980	Pa×s	313.15	Densiti...
η	0.0005980	Pa×s	323.15	Thermod...
η	0.0005978	Pa×s	323.15	Density...
η	0.0006040	Pa×s	323.15	Densiti...
η	0.0005984	Pa×s	323.15	Thermod...
η	0.0005200	Pa×s	333.15	Thermod...
η	0.0005195	Pa×s	333.15	Thermod...
ΔfusH	[2.68; 6.74]	kJ/mol	[186.10; 279.80]
ΔfusH	6.74	kJ/mol	186.10	NIST
ΔfusH	2.68	kJ/mol	279.80	NIST
ΔfusH	2.68	kJ/mol	279.80	NIST
ΔsubH	[27.60; 46.60]	kJ/mol	[186.00; 274.00]
ΔsubH	46.60	kJ/mol	186.00	NIST
ΔsubH	37.70	kJ/mol	248.00	NIST
ΔsubH	27.60	kJ/mol	251.50	NIST
ΔsubH	37.20	kJ/mol	273.00	NIST
ΔsubH	36.50	kJ/mol	274.00	NIST
ΔvapH	[29.60; 33.33]	kJ/mol	[298.00; 521.00]
ΔvapH	32.83	kJ/mol	298.00	Enthalp...
ΔvapH	33.33	kJ/mol	298.15	NIST
ΔvapH	32.20 ± 0.10	kJ/mol	313.00	NIST
ΔvapH	32.30 ± 0.10	kJ/mol	313.00	NIST
ΔvapH	32.30	kJ/mol	314.00	NIST
ΔvapH	32.70	kJ/mol	322.50	NIST
ΔvapH	32.90	kJ/mol	323.00	NIST
ΔvapH	31.90 ± 0.10	kJ/mol	323.00	NIST
ΔvapH	32.50	kJ/mol	323.00	NIST
ΔvapH	32.90	kJ/mol	324.00	NIST
ΔvapH	31.40 ± 0.10	kJ/mol	324.00	NIST
ΔvapH	31.90	kJ/mol	324.50	NIST
ΔvapH	33.10	kJ/mol	324.50	NIST
ΔvapH	31.10	kJ/mol	332.00	NIST
ΔvapH	31.20 ± 0.10	kJ/mol	333.00	NIST
ΔvapH	31.10 ± 0.10	kJ/mol	333.00	NIST
ΔvapH	32.80	kJ/mol	335.00	NIST
ΔvapH	31.00 ± 0.10	kJ/mol	338.00	NIST
ΔvapH	30.60 ± 0.10	kJ/mol	343.00	NIST
ΔvapH	30.30	kJ/mol	345.00	NIST
ΔvapH	30.40 ± 0.10	kJ/mol	346.00	NIST
ΔvapH	30.40 ± 0.10	kJ/mol	348.00	NIST
ΔvapH	30.10 ± 0.10	kJ/mol	353.00	NIST
ΔvapH	29.97	kJ/mol	353.90	NIST
ΔvapH	29.96	kJ/mol	353.90	KDB
ΔvapH	30.10 ± 0.10	kJ/mol	354.00	NIST
ΔvapH	30.10	kJ/mol	354.00	NIST
ΔvapH	30.00	kJ/mol	355.00	NIST
ΔvapH	30.90	kJ/mol	383.50	NIST
ΔvapH	32.20	kJ/mol	415.00	NIST
ΔvapH	29.60	kJ/mol	451.50	NIST
ΔvapH	29.60	kJ/mol	521.00	NIST
Pvap	[2.08; 362.80]	kPa	[263.15; 403.15]
Pvap	2.08	kPa	263.15	Isother...
Pvap	3.73	kPa	273.15	Excess ...
Pvap	3.73	kPa	273.15	Isother...
Pvap	3.73	kPa	273.15	Excess ...
Pvap	6.35	kPa	283.15	Excess ...
Pvap	6.35	kPa	283.15	Excess ...
Pvap	6.36	kPa	283.15	Isother...
Pvap	6.39	kPa	283.32	Isother...
Pvap	6.39	kPa	283.32	Isother...
Pvap	8.20	kPa	288.28	Isother...
Pvap	8.20	kPa	288.28	Isother...
Pvap	10.36	kPa	293.15	Excess ...
Pvap	10.36	kPa	293.15	Excess ...
Pvap	10.37	kPa	293.15	Isother...
Pvap	10.42	kPa	293.27	Isother...
Pvap	10.42	kPa	293.27	Isother...
Pvap	11.15	kPa	295.42	Vapor-L...
Pvap	11.16	kPa	295.45	Vapor-L...
Pvap	11.17	kPa	295.46	Vapor-L...
Pvap	11.33	kPa	295.72	Vapor-L...
Pvap	11.35	kPa	295.75	Vapor-L...
Pvap	11.63	kPa	296.22	Vapor-L...
Pvap	12.15	kPa	297.08	Vapor-L...
Pvap	12.16	kPa	297.13	Vapor-L...
Pvap	12.17	kPa	297.13	Vapor-L...
Pvap	12.61	kPa	297.86	Vapor-L...
Pvap	12.71	kPa	297.99	Vapor-L...
Pvap	13.04	kPa	298.15	Isother...
Pvap	13.04	kPa	298.15	Excess ...
Pvap	13.17	kPa	298.25	Isother...
Pvap	13.17	kPa	298.25	Isother...
Pvap	13.23	kPa	298.83	Vapor-L...
Pvap	13.80	kPa	299.75	Vapor-L...
Pvap	13.81	kPa	299.77	Vapor-L...
Pvap	14.52	kPa	300.85	Vapor-L...
Pvap	15.71	kPa	302.63	Vapor-L...
Pvap	16.06	kPa	302.92	Vapor-L...
Pvap	16.03	kPa	303.02	Vapor-L...
Pvap	16.40	kPa	303.15	Bubble ...
Pvap	16.11	kPa	303.15	Vapor-L...
Pvap	16.26	kPa	303.15	Isother...
Pvap	16.26	kPa	303.15	Excess ...
Pvap	16.26	kPa	303.15	Excess ...
Pvap	16.45	kPa	303.27	Isother...
Pvap	16.45	kPa	303.27	Isother...
Pvap	16.95	kPa	304.19	Vapor-L...
Pvap	17.04	kPa	304.38	Vapor-L...
Pvap	17.05	kPa	304.40	Vapor-L...
Pvap	17.07	kPa	304.42	Vapor-L...
Pvap	18.33	kPa	306.05	Vapor-L...
Pvap	18.60	kPa	306.40	Vapor-L...
Pvap	19.05	kPa	306.91	Vapor-L...
Pvap	19.40	kPa	307.45	Vapor-L...
Pvap	19.91	kPa	308.06	Vapor-L...
Pvap	20.00	kPa	308.07	Isobari...
Pvap	19.80	kPa	308.15	VLE and...
Pvap	20.16	kPa	308.27	Vapor-L...
Pvap	21.12	kPa	309.50	Vapor-L...
Pvap	21.56	kPa	309.90	Vapor-L...
Pvap	22.47	kPa	310.98	Vapor-L...
Pvap	23.89	kPa	312.48	Vapor-L...
Pvap	24.65	kPa	313.15	Excess ...
Pvap	24.65	kPa	313.15	Isother...
Pvap	24.56	kPa	313.15	Vapor-L...
Pvap	24.70	kPa	313.15	Bubble ...
Pvap	24.63	kPa	313.15	Vapor-L...
Pvap	24.65	kPa	313.15	Excess ...
Pvap	24.62	kPa	313.15	Vapor L...
Pvap	24.61	kPa	313.16	Vapor-L...
Pvap	24.97	kPa	313.24	Isother...
Pvap	24.97	kPa	313.24	Isother...
Pvap	24.95	kPa	313.40	Isobari...
Pvap	25.25	kPa	313.84	Vapor-L...
Pvap	26.47	kPa	315.01	Vapor-L...
Pvap	26.67	kPa	315.26	Vapor-L...
Pvap	27.43	kPa	315.76	Isobari...
Pvap	27.88	kPa	316.32	Vapor-L...
Pvap	29.23	kPa	317.51	Vapor-L...
Pvap	29.77	kPa	317.95	Determi...
Pvap	29.95	kPa	318.05	Isobari...
Pvap	30.03	kPa	318.19	Vapor-L...
Pvap	29.70	kPa	318.30	VLE and...
Pvap	30.09	kPa	318.31	Vapor-L...
Pvap	30.56	kPa	318.67	Vapor-L...
Pvap	31.93	kPa	319.81	Vapor-L...
Pvap	32.46	kPa	320.11	Isobari...
Pvap	33.27	kPa	320.87	Vapor-L...
Pvap	34.59	kPa	321.91	Vapor-L...
Pvap	34.69	kPa	321.99	Vapor-L...
Pvap	34.90	kPa	322.06	Isobari...
Pvap	35.95	kPa	322.94	Vapor-L...
Pvap	36.23	kPa	323.14	Vapor-L...
Pvap	36.27	kPa	323.15	Vapor-L...
Pvap	36.24	kPa	323.15	Excess ...
Pvap	36.24	kPa	323.15	Excess ...
Pvap	36.24	kPa	323.15	Isother...
Pvap	36.40	kPa	323.15	Bubble ...
Pvap	36.72	kPa	323.21	Isother...
Pvap	36.72	kPa	323.21	Isother...
Pvap	36.59	kPa	323.44	Vapor-L...
Pvap	37.23	kPa	323.88	Vapor-L...
Pvap	37.43	kPa	323.92	Isobari...
Pvap	37.33	kPa	323.95	Vapor-L...
Pvap	38.19	kPa	324.72	Isobari...
Pvap	38.28	kPa	324.73	Isobari...
Pvap	38.56	kPa	324.83	Vapor-L...
Pvap	40.00	kPa	325.65	Determi...
Pvap	39.94	kPa	325.66	Isobari...
Pvap	39.70	kPa	325.95	VLE and...
Pvap	40.45	kPa	326.12	Vapor-L...
Pvap	41.25	kPa	326.68	Vapor-L...
Pvap	42.42	kPa	327.32	Isobari...
Pvap	42.68	kPa	327.61	Vapor-L...
Pvap	43.51	kPa	328.16	Vapor-L...
Pvap	43.97	kPa	328.43	Vapor-L...
Pvap	44.91	kPa	328.90	Isobari...
Pvap	45.40	kPa	329.32	Vapor-L...
Pvap	45.43	kPa	329.35	Vapor-L...
Pvap	46.59	kPa	330.05	Vapor-L...
Pvap	47.45	kPa	330.44	Isobari...
Pvap	48.07	kPa	330.94	Vapor-L...
Pvap	49.32	kPa	331.68	Vapor-L...
Pvap	49.68	kPa	331.90	Vapor-L...
Pvap	49.92	kPa	331.94	Isobari...
Pvap	49.89	kPa	332.02	Vapor-L...
Pvap	50.00	kPa	332.08	Isobari...
Pvap	49.70	kPa	332.10	VLE and...
Pvap	50.60	kPa	332.41	Vapor-L...
Pvap	51.87	kPa	333.11	Vapor-L...
Pvap	51.92	kPa	333.15	Vapor-L...
Pvap	52.00	kPa	333.15	Bubble ...
Pvap	51.85	kPa	333.15	Excess ...
Pvap	51.85	kPa	333.15	Isother...
Pvap	51.85	kPa	333.15	Excess ...
Pvap	51.90	kPa	333.16	Vapor-L...
Pvap	51.90	kPa	333.17	Vapor-L...
Pvap	52.48	kPa	333.21	Isother...
Pvap	52.48	kPa	333.21	Isother...
Pvap	52.43	kPa	333.33	Isobari...
Pvap	53.33	kPa	333.77	Determi...
Pvap	53.15	kPa	333.83	Vapor-L...
Pvap	53.19	kPa	333.86	Vapor-L...
Pvap	53.30	kPa	333.96	Isobari...
Pvap	54.47	kPa	334.53	Vapor-L...
Pvap	54.76	kPa	334.60	Isobari...
Pvap	55.85	kPa	335.26	Vapor-L...
Pvap	56.56	kPa	335.64	Vapor-L...
Pvap	57.19	kPa	335.95	Vapor-L...
Pvap	57.44	kPa	335.99	Isobari...
Pvap	58.63	kPa	336.70	Vapor-L...
Pvap	58.85	kPa	336.85	Determi...
Pvap	59.98	kPa	337.31	Isobari...
Pvap	59.96	kPa	337.36	Vapor-L...
Pvap	59.70	kPa	337.45	VLE and...
Pvap	60.49	kPa	337.59	Isobari...
Pvap	61.39	kPa	338.06	Vapor-L...
Pvap	61.40	kPa	338.06	Vapor-L...
Pvap	61.50	kPa	338.15	Phase e...
Pvap	61.56	kPa	338.16	Vapor-L...
Pvap	62.44	kPa	338.50	Isobari...
Pvap	62.63	kPa	338.65	Vapor-L...
Pvap	62.64	kPa	338.67	Vapor-L...
Pvap	63.95	kPa	339.29	Vapor-L...
Pvap	64.86	kPa	339.65	Isobari...
Pvap	65.29	kPa	339.92	Vapor-L...
Pvap	66.66	kPa	340.43	Determi...
Pvap	66.63	kPa	340.54	Vapor-L...
Pvap	67.47	kPa	340.81	Isobari...
Pvap	67.95	kPa	341.12	Vapor-L...
Pvap	69.29	kPa	341.72	Vapor-L...
Pvap	69.94	kPa	341.92	Isobari...
Pvap	69.95	kPa	341.96	Isobari...
Pvap	69.80	kPa	342.05	VLE and...
Pvap	70.65	kPa	342.32	Vapor-L...
Pvap	71.93	kPa	342.88	Vapor-L...
Pvap	72.45	kPa	342.99	Isobari...
Pvap	72.39	kPa	343.15	Excess ...
Pvap	72.50	kPa	343.15	Bubble ...
Pvap	72.40	kPa	343.15	Excess ...
Pvap	72.39	kPa	343.15	Isother...
Pvap	72.60	kPa	343.15	Vapor-L...
Pvap	72.53	kPa	343.16	Vapor-L...
Pvap	72.98	kPa	343.18	Isother...
Pvap	72.98	kPa	343.18	Isother...
Pvap	73.25	kPa	343.43	Vapor-L...
Pvap	74.01	kPa	343.68	Isobari...
Pvap	74.96	kPa	344.05	Isobari...
Pvap	74.73	kPa	344.05	Vapor-L...
Pvap	75.07	kPa	344.09	Isobari...
Pvap	75.96	kPa	344.55	Vapor-L...
Pvap	77.27	kPa	345.08	Vapor-L...
Pvap	77.54	kPa	345.11	Isobari...
Pvap	77.94	kPa	345.42	Vapor-L...
Pvap	78.76	kPa	345.69	Vapor-L...
Pvap	79.92	kPa	346.07	Isobari...
Pvap	79.99	kPa	346.11	Determi...
Pvap	80.00	kPa	346.13	Isobari...
Pvap	80.00	kPa	346.18	Vapor-L...
Pvap	79.90	kPa	346.25	VLE and...
Pvap	81.20	kPa	346.58	Isobari...
Pvap	81.25	kPa	346.67	Vapor-L...
Pvap	82.52	kPa	347.06	Isobari...
Pvap	82.56	kPa	347.18	Vapor-L...
Pvap	82.57	kPa	347.18	Vapor-L...
Pvap	83.89	kPa	347.69	Vapor-L...
Pvap	85.03	kPa	348.01	Isobari...
Pvap	84.73	kPa	348.05	Vapor-L...
Pvap	84.70	kPa	348.15	Phase e...
Pvap	85.23	kPa	348.19	Vapor-L...
Pvap	86.49	kPa	348.65	Vapor-L...
Pvap	87.27	kPa	348.86	Isobari...
Pvap	87.65	kPa	349.15	Determi...
Pvap	87.93	kPa	349.19	Vapor-L...
Pvap	89.43	kPa	349.72	Vapor-L...
Pvap	89.99	kPa	349.84	Isobari...
Pvap	90.05	kPa	350.00	VLE and...
Pvap	90.64	kPa	350.18	Vapor-L...
Pvap	90.87	kPa	350.25	Vapor-L...
Pvap	92.07	kPa	350.67	Vapor-L...
Pvap	92.48	kPa	350.73	Isobari...
Pvap	93.27	kPa	351.10	Vapor-L...
Pvap	93.32	kPa	351.12	Determi...
Pvap	94.84	kPa	351.55	Isobari...
Pvap	94.63	kPa	351.57	Vapor-L...
Pvap	95.17	kPa	351.72	Isobari...
Pvap	95.92	kPa	352.01	Vapor-L...
Pvap	97.23	kPa	352.45	Vapor-L...
Pvap	98.57	kPa	352.90	Vapor-L...
Pvap	99.11	kPa	353.14	Isother...
Pvap	99.11	kPa	353.14	Isother...
Pvap	98.87	kPa	353.15	Excess ...
Pvap	99.31	kPa	353.15	Vapor-L...
Pvap	98.85	kPa	353.15	Isother...
Pvap	98.87	kPa	353.15	Excess ...
Pvap	99.95	kPa	353.36	Vapor-L...
Pvap	101.30	kPa	353.70	Isobari...
Pvap	101.30	kPa	353.73	Isobari...
Pvap	101.33	kPa	353.73	Isobari...
Pvap	101.30	kPa	353.82	A New T...
Pvap	101.30	kPa	353.82	A new a...
Pvap	101.33	kPa	353.85	Vapor L...
Pvap	101.30	kPa	353.94	Isobari...
Pvap	101.75	kPa	354.05	VLE and...
Pvap	102.34	kPa	354.11	Isobari...
Pvap	132.35	kPa	363.15	Excess ...
Pvap	132.35	kPa	363.15	Excess ...
Pvap	132.33	kPa	363.15	Isother...
Pvap	362.80	kPa	403.15	Isother...
n0	[1.41516; 1.43193]		[283.15; 313.15]
n0	1.43193		283.15	Density...
n0	1.42350		293.15	Solubil...
n0	1.42590		293.15	Liquid-...
n0	1.42660		293.15	Solubil...
n0	1.42650		293.15	Vapour ...
n0	1.42633		293.15	Mixing ...
n0	1.42690		293.20	Phase E...
n0	1.42630		293.20	Liquid ...
n0	1.42354		298.15	KDB
n0	1.42350		298.15	Phase e...
n0	1.42508		298.15	Phase e...
n0	1.42360		298.15	Experim...
n0	1.42320		298.15	Azeotro...
n0	1.42508		298.15	Vapor l...
n0	1.42354		298.15	Mixing ...
n0	1.42360		298.15	Density...
n0	1.42403		298.15	(Liquid...
n0	1.42360		298.15	Separat...
n0	1.42360		298.15	(Liquid...
n0	1.42356		298.15	Applica...
n0	1.42378		298.15	Liquid ...
n0	1.42350		298.15	Bubble ...
n0	1.42350		298.15	Bubble-...
n0	1.42360		298.15	Solubil...
n0	1.42360		298.15	Solubil...
n0	1.42350		298.15	Vapor l...
n0	1.42360		298.15	Solubil...
n0	1.42350		298.15	Activit...
n0	1.42360		298.15	Liquid ...
n0	1.42360		298.15	Density...
n0	1.42360		298.15	Liquid ...
n0	1.42650		298.15	Vapor L...
n0	1.42403		298.15	Liquid-...
n0	1.42350		298.15	Densiti...
n0	1.42073		303.15	Mixing ...
n0	1.42050		308.15	Topolog...
n0	1.41516		313.15	Density...
ρl	[89.90; 788.30]	kg/m3	[287.00; 698.50]
ρl	788.30	kg/m3	287.00	Design ...
ρl	783.00	kg/m3	288.15	Effect ...
ρl	778.54	kg/m3	293.00	Volumet...
ρl	779.00	kg/m3	293.00	KDB
ρl	778.20	kg/m3	293.10	Vapor-L...
ρl	778.50	kg/m3	293.15	Partial...
ρl	778.51	kg/m3	293.15	Excess ...
ρl	779.00	kg/m3	293.15	Effect ...
ρl	778.56	kg/m3	293.15	Excess ...
ρl	778.70	kg/m3	293.15	Densiti...
ρl	779.00	kg/m3	293.15	Thermop...
ρl	778.41	kg/m3	293.15	Isother...
ρl	778.00	kg/m3	293.15	Thermop...
ρl	778.80	kg/m3	293.15	Densiti...
ρl	778.70	kg/m3	293.15	Densiti...
ρl	778.71	kg/m3	293.15	Thermod...
ρl	773.88	kg/m3	298.10	Excess ...
ρl	773.65	kg/m3	298.15	Experim...
ρl	776.11	kg/m3	298.15	Quatern...
ρl	773.96	kg/m3	298.15	Thermod...
ρl	773.80	kg/m3	298.15	Density...
ρl	774.02	kg/m3	298.15	Thermod...
ρl	773.90	kg/m3	298.15	Densiti...
ρl	773.81	kg/m3	298.15	Volumet...
ρl	773.94	kg/m3	298.15	Topolog...
ρl	774.00	kg/m3	298.15	Effect ...
ρl	773.84	kg/m3	298.15	Excess ...
ρl	773.88	kg/m3	298.15	Quatern...
ρl	773.94	kg/m3	298.15	Excess ...
ρl	773.93	kg/m3	298.15	Viscosi...
ρl	773.98	kg/m3	298.15	Vapor-L...
ρl	773.50	kg/m3	298.15	Measure...
ρl	773.87	kg/m3	298.15	Volumet...
ρl	773.88	kg/m3	298.15	(Liquid...
ρl	773.86	kg/m3	298.15	Volumet...
ρl	773.92	kg/m3	298.15	Excess ...
ρl	773.86	kg/m3	298.15	Thermod...
ρl	773.94	kg/m3	298.15	Excess ...
ρl	775.00	kg/m3	298.15	Isother...
ρl	773.70	kg/m3	298.15	Fluid P...
ρl	773.90	kg/m3	298.15	Densiti...
ρl	774.00	kg/m3	298.15	Effect ...
ρl	773.80	kg/m3	298.15	Viscosi...
ρl	773.90	kg/m3	298.15	Densiti...
ρl	774.00	kg/m3	298.15	Liquid-...
ρl	779.00	kg/m3	298.15	Liquid ...
ρl	774.00	kg/m3	298.15	Liquid-...
ρl	773.78	kg/m3	298.15	Densiti...
ρl	773.92	kg/m3	298.15	Binary ...
ρl	773.85	kg/m3	298.20	Apparen...
ρl	769.13	kg/m3	303.00	Volumet...
ρl	769.00	kg/m3	303.15	Thermop...
ρl	769.12	kg/m3	303.15	Volumet...
ρl	769.12	kg/m3	303.15	Volumet...
ρl	769.10	kg/m3	303.15	Studies...
ρl	769.11	kg/m3	303.15	Excess ...
ρl	769.30	kg/m3	303.15	Thermod...
ρl	768.80	kg/m3	303.15	Densiti...
ρl	768.90	kg/m3	303.15	Volumet...
ρl	769.12	kg/m3	303.15	Volumet...
ρl	769.30	kg/m3	303.15	Densiti...
ρl	769.21	kg/m3	303.15	Excess ...
ρl	769.00	kg/m3	303.15	Effect ...
ρl	763.70	kg/m3	305.90	Design ...
ρl	764.45	kg/m3	308.15	Excess ...
ρl	764.50	kg/m3	308.15	Densiti...
ρl	764.30	kg/m3	308.15	Densiti...
ρl	765.00	kg/m3	308.15	Total P...
ρl	764.00	kg/m3	308.15	Densiti...
ρl	764.36	kg/m3	308.15	Excess ...
ρl	764.35	kg/m3	308.15	Volumet...
ρl	759.60	kg/m3	313.00	Volumet...
ρl	759.00	kg/m3	313.15	Thermop...
ρl	759.56	kg/m3	313.15	Volumet...
ρl	759.30	kg/m3	313.15	Densiti...
ρl	760.00	kg/m3	313.15	Effect ...
ρl	759.57	kg/m3	313.15	Excess ...
ρl	759.41	kg/m3	313.15	Thermod...
ρl	760.00	kg/m3	313.15	Thermop...
ρl	759.20	kg/m3	313.15	Volumet...
ρl	759.70	kg/m3	313.15	Densiti...
ρl	759.80	kg/m3	313.15	Excess ...
ρl	759.52	kg/m3	313.15	Studies...
ρl	754.74	kg/m3	318.15	Volumet...
ρl	754.60	kg/m3	318.15	Thermod...
ρl	754.40	kg/m3	318.15	Densiti...
ρl	749.94	kg/m3	323.00	Volumet...
ρl	749.88	kg/m3	323.15	Volumet...
ρl	751.00	kg/m3	323.15	Effect ...
ρl	748.70	kg/m3	323.15	Volumet...
ρl	749.76	kg/m3	323.15	Thermod...
ρl	749.50	kg/m3	323.15	Densiti...
ρl	752.10	kg/m3	324.90	Design ...
ρl	741.00	kg/m3	333.15	Effect ...
ρl	731.00	kg/m3	343.15	Effect ...
ρl	731.80	kg/m3	351.00	Design ...
ρl	704.30	kg/m3	375.00	Design ...
ρl	686.70	kg/m3	394.80	Design ...
ρl	666.50	kg/m3	416.60	Design ...
ρl	646.20	kg/m3	431.90	Design ...
ρl	620.20	kg/m3	452.40	Design ...
ρl	595.50	kg/m3	475.10	Design ...
ρl	573.50	kg/m3	488.40	Design ...
ρl	546.30	kg/m3	504.40	Design ...
ρl	527.50	kg/m3	513.90	Design ...
ρl	510.30	kg/m3	522.60	Design ...
ρl	487.00	kg/m3	531.90	Design ...
ρl	454.50	kg/m3	543.00	Design ...
ρl	426.20	kg/m3	553.20	Design ...
ρl	365.60	kg/m3	561.70	Design ...
ρl	259.50	kg/m3	572.10	Design ...
ρl	187.00	kg/m3	584.20	Design ...
ρl	167.00	kg/m3	592.50	Design ...
ρl	149.30	kg/m3	603.60	Design ...
ρl	133.00	kg/m3	618.80	Design ...
ρl	118.30	kg/m3	635.00	Design ...
ρl	109.80	kg/m3	654.20	Design ...
ρl	96.50	kg/m3	672.30	Design ...
ρl	92.00	kg/m3	687.50	Design ...
ρl	89.90	kg/m3	698.50	Design ...
D*i	[0.00; 0.00]	m2/s	[308.16; 328.15]
D*i	0.00	m2/s	308.16	Viscous...
D*i	0.00	m2/s	308.17	Viscous...
D*i	0.00	m2/s	318.22	Viscous...
D*i	0.00	m2/s	318.25	Viscous...
D*i	0.00	m2/s	328.13	Viscous...
D*i	0.00	m2/s	328.15	Viscous...
ΔfusS	[9.57; 36.20]	J/mol×K	[186.10; 279.80]
ΔfusS	36.20	J/mol×K	186.10	NIST
ΔfusS	9.57	J/mol×K	279.80	NIST
csound,fluid	[1133.70; 1327.80]	m/s	[283.15; 323.15]
csound,fluid	1327.80	m/s	283.15	Speeds ...
csound,fluid	1278.60	m/s	293.15	Tempera...
csound,fluid	1279.00	m/s	293.15	Acousti...
csound,fluid	1278.55	m/s	293.15	Volumet...
csound,fluid	1254.40	m/s	298.15	Speeds ...
csound,fluid	1254.00	m/s	298.15	Densiti...
csound,fluid	1255.00	m/s	298.15	Thermod...
csound,fluid	1253.86	m/s	298.15	Volumet...
csound,fluid	1253.90	m/s	298.15	Tempera...
csound,fluid	1229.34	m/s	303.15	Volumet...
csound,fluid	1229.30	m/s	303.15	Tempera...
csound,fluid	1205.05	m/s	308.15	Volumet...
csound,fluid	1205.10	m/s	308.15	Tempera...
csound,fluid	1212.00	m/s	308.15	Thermod...
csound,fluid	1212.00	m/s	308.15	Densiti...
csound,fluid	1181.03	m/s	313.15	Volumet...
csound,fluid	1181.00	m/s	313.15	Tempera...
csound,fluid	1181.10	m/s	313.15	Speeds ...
csound,fluid	1157.29	m/s	318.15	Volumet...
csound,fluid	1157.30	m/s	318.15	Tempera...
csound,fluid	1133.70	m/s	323.15	Tempera...
csound,fluid	1133.73	m/s	323.15	Volumet...
γ	[0.02; 0.03]	N/m	[279.33; 337.93]
γ	0.03	N/m	279.33	Surface...
γ	0.03	N/m	282.82	Surface...
γ	0.03	N/m	283.15	Thermop...
γ	0.03	N/m	287.81	Surface...
γ	0.03	N/m	288.15	Interfa...
γ	0.03	N/m	293.15	Surface...
γ	0.03	N/m	293.15	Surface...
γ	0.03	N/m	293.20	KDB
γ	0.02	N/m	297.82	Surface...
γ	0.02	N/m	298.15	Thermop...
γ	0.02	N/m	298.15	Surface...
γ	0.02	N/m	298.15	Surface...
γ	0.02	N/m	298.15	Interfa...
γ	0.02	N/m	303.15	Surface...
γ	0.02	N/m	303.15	Surface...
γ	0.02	N/m	307.86	Surface...
γ	0.02	N/m	308.15	Surface...
γ	0.02	N/m	308.15	Interfa...
γ	0.02	N/m	308.15	Surface...
γ	0.02	N/m	313.15	Surface...
γ	0.02	N/m	313.15	Surface...
γ	0.02	N/m	313.15	Thermop...
γ	0.02	N/m	317.86	Surface...
γ	0.02	N/m	318.15	Surface...
γ	0.02	N/m	318.15	Surface...
γ	0.02	N/m	318.15	Interfa...
γ	0.02	N/m	323.15	Surface...
γ	0.02	N/m	323.15	Surface...
γ	0.02	N/m	327.88	Surface...
γ	0.02	N/m	328.15	Interfa...
γ	0.02	N/m	337.93	Surface...
ΔvapS	111.80	J/mol×K	298.15	NIST
λ	[0.11; 0.12]	W/m×K	[280.83; 318.95]
λ	0.12	W/m×K	280.83	Thermal...
λ	0.12	W/m×K	281.00	Thermal...
λ	0.12	W/m×K	281.15	Thermal...
λ	0.12	W/m×K	295.53	Thermal...
λ	0.12	W/m×K	295.70	Thermal...
λ	0.12	W/m×K	295.83	Thermal...
λ	0.12	W/m×K	300.84	Thermal...
λ	0.12	W/m×K	301.00	Thermal...
λ	0.12	W/m×K	301.14	Thermal...
λ	0.11	W/m×K	318.66	Thermal...
λ	0.11	W/m×K	318.82	Thermal...
λ	0.11	W/m×K	318.95	Thermal...

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboil	[312.78; 350.53]	K	[24.08; 91.68]
Tboil	312.78	K	24.08	A novel...
Tboil	318.96	K	30.70	A novel...
Tboil	325.07	K	38.72	A novel...
Tboil	330.32	K	46.85	A novel...
Tboil	335.01	K	55.20	A novel...
Tboil	338.21	K	61.52	A novel...
Tboil	341.67	K	69.06	A novel...
Tboil	345.37	K	77.87	A novel...
Tboil	348.28	K	85.44	A novel...
Tboil	350.53	K	91.68	A novel...

Datasets

1. Viscosity, Pa*s (3)
2. Mass density, kg/m3 (6)

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
303.10	2930.00	0.0009
305.20	140.00	0.0008
305.10	960.00	0.0008
305.20	1960.00	0.0008
305.20	3940.00	0.0008
313.80	2920.00	0.0007
323.70	150.00	0.0006
324.00	1020.00	0.0006
323.70	1990.00	0.0006
323.70	4000.00	0.0006
348.90	140.00	0.0004
348.90	990.00	0.0004
348.90	2080.00	0.0004
348.90	3030.00	0.0005
348.90	3930.00	0.0004
373.70	970.00	0.0003
373.70	2020.00	0.0003
373.70	2930.00	0.0003
373.70	3960.00	0.0003
398.20	960.00	0.0003
398.10	2000.00	0.0003
398.20	2940.00	0.0003
398.10	4010.00	0.0003
422.40	960.00	0.0002
422.50	1970.00	0.0002
422.50	2960.00	0.0002
422.50	3960.00	0.0002
447.50	1010.00	0.0002
447.60	2040.00	0.0002
447.70	3010.00	0.0002
447.70	4000.00	0.0002
473.40	1930.00	0.0001
473.30	3000.00	0.0001
473.40	3930.00	0.0001
498.20	3020.00	0.0001
497.90	3050.00	0.0001
498.10	3980.00	0.0001
498.30	4020.00	0.0001
523.00	3050.00	0.0001
523.00	3970.00	0.0001
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Viscosity, Pa*s - Liquid
690.00	313.20	0.0007
690.00	333.20	0.0005
690.00	353.20	0.0004
690.00	373.20	0.0003
690.00	393.20	0.0002
5000.00	313.20	0.0008
5000.00	333.20	0.0006
5000.00	353.20	0.0004
5000.00	373.20	0.0003
5000.00	393.20	0.0003
10000.00	313.20	0.0008
10000.00	333.20	0.0006
10000.00	353.20	0.0005
10000.00	373.20	0.0004
10000.00	393.20	0.0003
20000.00	313.20	0.0009
20000.00	333.20	0.0007
20000.00	353.20	0.0005
20000.00	373.20	0.0004
20000.00	393.20	0.0003
30000.00	313.20	0.0010
30000.00	333.20	0.0008
30000.00	353.20	0.0006
30000.00	373.20	0.0005
30000.00	393.20	0.0004
40000.00	313.20	0.0011
40000.00	333.20	0.0008
40000.00	353.20	0.0007
40000.00	373.20	0.0005
40000.00	393.20	0.0004
50000.00	313.20	0.0012
50000.00	333.20	0.0009
50000.00	353.20	0.0007
50000.00	373.20	0.0006
50000.00	393.20	0.0005
60000.00	313.20	0.0013
60000.00	333.20	0.0010
60000.00	353.20	0.0008
60000.00	373.20	0.0006
60000.00	393.20	0.0005
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
298.15	100.00	0.0009
298.15	4000.00	0.0009
298.15	7600.00	0.0010
298.15	13700.00	0.0010
298.15	20900.00	0.0011
298.15	27700.00	0.0012
298.15	34700.00	0.0013
318.15	6895.00	0.0007
318.15	13790.00	0.0007
318.15	20680.00	0.0008
318.15	27580.00	0.0008
318.15	34470.00	0.0009
318.15	41370.00	0.0010
318.15	48260.00	0.0010
318.15	55160.00	0.0011
318.15	62050.00	0.0012
323.15	100.00	0.0006
323.15	7200.00	0.0007
323.15	14200.00	0.0007
323.15	21100.00	0.0008
323.15	27700.00	0.0008
323.15	40000.00	0.0010
323.15	48200.00	0.0010
323.15	50900.00	0.0011
323.15	52300.00	0.0011
323.15	54300.00	0.0011
323.15	55000.00	0.0009
333.15	100.00	0.0005
333.15	3800.00	0.0005
333.15	6895.00	0.0005
333.15	7300.00	0.0006
333.15	13790.00	0.0006
333.15	14100.00	0.0006
333.15	20600.00	0.0007
333.15	20680.00	0.0006
333.15	27580.00	0.0007
333.15	27800.00	0.0007
333.15	34470.00	0.0008
333.15	34700.00	0.0008
333.15	41370.00	0.0008
333.15	42000.00	0.0008
333.15	48260.00	0.0009
333.15	49000.00	0.0009
333.15	53500.00	0.0009
333.15	55160.00	0.0009
333.15	62050.00	0.0010
348.15	6895.00	0.0005
348.15	13790.00	0.0005
348.15	20680.00	0.0005
348.15	27580.00	0.0006
348.15	34470.00	0.0006
348.15	41370.00	0.0007
348.15	48260.00	0.0007
348.15	55160.00	0.0008
348.15	62050.00	0.0008
363.15	6895.00	0.0004
363.15	13790.00	0.0004
363.15	20680.00	0.0005
363.15	27580.00	0.0005
363.15	34470.00	0.0005
363.15	41370.00	0.0006
363.15	48260.00	0.0006
363.15	55160.00	0.0007
363.15	62050.00	0.0007
388.15	6895.00	0.0003
388.15	13790.00	0.0003
388.15	20680.00	0.0004
388.15	27580.00	0.0004
388.15	34470.00	0.0004
388.15	41370.00	0.0004
388.15	48260.00	0.0005
388.15	55160.00	0.0005
388.15	62050.00	0.0005
413.15	6895.00	0.0002
413.15	13790.00	0.0003
413.15	20680.00	0.0003
413.15	27580.00	0.0003
413.15	34470.00	0.0003
413.15	41370.00	0.0004
413.15	48260.00	0.0004
413.15	55160.00	0.0004
413.15	62050.00	0.0004
Reference

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	773.6
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.15	99.46	778.632
293.15	1102.03	779.471
293.15	2002.37	780.22
293.15	4003.86	781.856
293.15	6003.84	783.454
293.15	8003.30	785.025
293.15	10042.20	786.595
293.15	12045.50	788.105
293.15	13918.70	789.495
293.15	15982.40	790.995
293.15	17946.40	792.401
293.15	20017.10	793.855
313.15	102.48	759.667
313.15	1139.02	760.675
313.15	2012.18	761.509
313.15	4102.38	763.47
313.15	5932.83	765.157
313.15	7910.50	766.936
313.15	10017.50	768.784
313.15	12069.20	770.545
313.15	13964.70	772.137
313.15	15901.80	773.737
313.15	17955.80	775.394
313.15	20142.40	777.123
333.15	1112.41	741.367
333.15	2043.58	742.401
333.15	3987.96	744.517
333.15	5966.83	746.613
333.15	8141.84	748.853
333.15	10007.20	750.72
333.15	11993.60	752.664
333.15	14092.70	754.666
333.15	15962.90	756.414
333.15	17994.70	758.261
333.15	19860.60	759.929
353.15	1109.91	721.547
353.15	1973.18	722.669
353.15	4000.02	725.242
353.15	6001.27	727.698
353.15	8046.51	730.125
353.15	10046.10	732.423
353.15	11820.50	734.413
353.15	13860.00	736.633
353.15	15939.70	738.835
353.15	18023.40	740.978
353.15	20002.80	742.965
373.15	1115.51	701.065
373.15	1950.06	702.346
373.15	4154.07	705.638
373.15	6126.03	708.455
373.15	8029.39	711.079
373.15	9951.24	713.63
373.15	12097.10	716.383
373.15	13877.00	718.592
373.15	16148.10	721.319
373.15	18077.70	723.568
373.15	19877.00	725.607
393.15	1162.91	679.792
393.15	1960.31	681.265
393.15	3901.42	684.723
393.15	5983.91	688.253
393.15	7986.39	691.487
393.15	9903.28	694.452
393.15	11974.70	697.527
393.15	13821.00	700.163
393.15	16029.30	703.195
393.15	18027.30	705.845
393.15	20003.70	708.371
413.15	1196.72	657.32
413.15	2172.63	659.527
413.15	4146.43	663.767
413.15	6122.26	667.756
413.15	8132.63	671.583
413.15	10013.20	674.989
413.15	11993.30	678.397
413.15	14003.50	681.703
413.15	16052.90	684.936
413.15	18098.20	688.022
413.15	19934.80	690.694
433.15	1086.72	632.817
433.15	2070.58	635.63
433.15	4050.34	640.931
433.15	6077.00	645.937
433.15	8181.71	650.742
433.15	10076.70	654.811
433.15	12111.10	658.913
433.15	13890.30	662.325
433.15	15958.80	666.096
433.15	18073.30	669.76
433.15	20009.80	672.969
453.15	2100.81	609.942
453.15	4117.30	616.844
453.15	6121.33	623.004
453.15	8117.44	628.596
453.15	9915.40	633.254
453.15	11931.40	638.115
453.15	13934.70	642.628
453.15	15959.00	646.918
453.15	18103.10	651.206
453.15	19890.50	654.601
473.15	2403.47	582.448
473.15	3924.93	589.431
473.15	6045.23	597.933
473.15	8093.25	605.148
473.15	9884.30	610.832
473.15	11911.40	616.733
473.15	13942.60	622.171
473.15	16018.50	627.319
473.15	18132.60	632.216
473.15	20025.00	636.335
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
288.15	100.00	782.7
288.15	1000.00	783.7
288.15	5000.00	787.0
288.15	10000.00	790.7
288.15	15000.00	794.1
298.15	100.00	773.2
298.15	1000.00	774.0
298.15	5000.00	777.6
298.15	10000.00	781.8
298.15	15000.00	785.6
298.15	20000.00	789.3
298.15	25000.00	792.9
298.15	30000.00	796.8
298.15	35000.00	799.7
308.15	100.00	763.6
308.15	1000.00	764.5
308.15	5000.00	768.2
308.15	10000.00	772.6
308.15	15000.00	776.8
308.15	20000.00	780.8
308.15	25000.00	784.6
308.15	30000.00	788.3
308.15	35000.00	791.8
308.15	40000.00	795.2
318.15	100.00	754.0
318.15	1000.00	755.0
318.15	5000.00	759.0
318.15	10000.00	763.7
318.15	15000.00	767.9
318.15	20000.00	772.4
318.15	25000.00	776.4
318.15	30000.00	780.3
318.15	35000.00	784.1
318.15	40000.00	787.7
318.15	45000.00	791.1
318.15	50000.00	794.4
328.15	100.00	744.4
328.15	1000.00	745.4
328.15	5000.00	749.7
328.15	10000.00	754.7
328.15	15000.00	759.5
328.15	20000.00	764.0
328.15	25000.00	768.2
328.15	30000.00	772.3
328.15	35000.00	776.1
328.15	40000.00	779.9
328.15	45000.00	783.5
328.15	50000.00	787.0
338.15	100.00	734.5
338.15	1000.00	735.6
338.15	5000.00	740.2
338.15	10000.00	745.7
338.15	15000.00	750.7
338.15	20000.00	755.5
338.15	25000.00	760.0
338.15	30000.00	764.3
338.15	35000.00	768.4
338.15	40000.00	772.3
338.15	45000.00	776.0
338.15	50000.00	779.7
338.15	55000.00	783.2
348.15	100.00	724.6
348.15	1000.00	725.7
348.15	5000.00	730.8
348.15	10000.00	736.5
348.15	15000.00	741.9
348.15	20000.00	747.0
348.15	25000.00	751.7
348.15	30000.00	756.2
348.15	35000.00	760.5
348.15	40000.00	764.6
348.15	45000.00	768.6
348.15	50000.00	772.3
348.15	55000.00	776.0
358.15	100.00	714.3
358.15	1000.00	715.6
358.15	5000.00	720.9
358.15	10000.00	727.2
358.15	15000.00	732.9
358.15	20000.00	738.3
358.15	25000.00	743.3
358.15	30000.00	748.1
358.15	35000.00	752.6
358.15	40000.00	757.0
358.15	45000.00	761.1
358.15	50000.00	765.0
358.15	55000.00	768.9
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.15	100.00	788.0
283.15	1000.00	788.7
283.15	2000.00	789.5
283.15	5000.00	791.8
293.15	100.00	778.8
293.15	1000.00	779.5
293.15	2000.00	780.4
293.15	5000.00	782.8
293.15	10000.00	786.6
293.15	15000.00	790.4
293.15	20000.00	793.9
313.15	100.00	759.8
313.15	1000.00	760.6
313.15	2000.00	761.5
313.15	5000.00	764.4
313.15	10000.00	768.7
313.15	15000.00	772.9
313.15	20000.00	776.9
333.15	100.00	740.5
333.15	1000.00	741.5
333.15	2000.00	742.6
333.15	5000.00	745.8
333.15	10000.00	750.9
333.15	15000.00	755.6
333.15	20000.00	760.1
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.15	100.00	778.4
293.15	1000.00	779.1
293.15	2000.00	779.9
293.15	5000.00	782.4
293.15	10000.00	786.3
293.15	15000.00	789.9
293.15	20000.00	793.4
303.15	100.00	769.0
303.15	1000.00	769.8
303.15	2000.00	770.7
303.15	5000.00	773.3
303.15	10000.00	777.5
303.15	15000.00	781.3
303.15	20000.00	785.1
303.15	30000.00	792.1
303.15	40000.00	798.5
313.15	100.00	759.7
313.15	1000.00	760.3
313.15	2000.00	761.2
313.15	5000.00	764.0
313.15	10000.00	768.4
313.15	15000.00	772.6
313.15	20000.00	776.6
313.15	30000.00	784.1
313.15	40000.00	790.9
323.15	100.00	750.1
323.15	1000.00	750.8
323.15	2000.00	751.8
323.15	5000.00	754.8
323.15	10000.00	759.5
323.15	15000.00	763.9
323.15	20000.00	768.2
323.15	30000.00	776.1
323.15	40000.00	783.2
333.15	100.00	740.3
333.15	1000.00	741.1
333.15	2000.00	742.2
333.15	5000.00	745.5
333.15	10000.00	750.5
333.15	15000.00	755.3
333.15	20000.00	759.7
333.15	30000.00	768.1
333.15	40000.00	775.6
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
318.15	6895.00	761.5
318.15	13789.00	767.7
318.15	20684.00	773.8
318.15	27579.00	779.0
318.15	34474.00	784.1
318.15	41369.00	788.7
318.15	48263.00	793.4
318.15	55158.00	797.4
318.15	62053.00	801.4
333.15	6895.00	747.3
333.15	13789.00	754.1
333.15	20684.00	760.5
333.15	27579.00	766.5
333.15	34474.00	772.0
333.15	41369.00	777.0
333.15	48263.00	781.7
333.15	55158.00	786.3
333.15	62053.00	790.7
348.15	6895.00	733.6
348.15	13789.00	741.2
348.15	20684.00	748.2
348.15	27579.00	754.5
348.15	34474.00	760.5
348.15	41369.00	766.1
348.15	48263.00	771.4
348.15	55158.00	776.2
348.15	62053.00	781.1
363.15	6895.00	719.6
363.15	13789.00	727.9
363.15	20684.00	735.7
363.15	27579.00	742.8
363.15	34474.00	749.1
363.15	41369.00	755.3
363.15	48263.00	760.7
363.15	55158.00	765.8
363.15	62053.00	771.0
388.15	6895.00	694.7
388.15	13789.00	705.0
388.15	20684.00	713.9
388.15	27579.00	721.9
388.15	34474.00	729.2
388.15	41369.00	736.0
388.15	48263.00	742.2
388.15	55158.00	747.8
388.15	62053.00	753.2
413.15	6895.00	669.7
413.15	13789.00	682.1
413.15	20684.00	692.5
413.15	27579.00	701.8
413.15	34474.00	710.1
413.15	41369.00	717.7
413.15	48263.00	724.9
413.15	55158.00	731.2
413.15	62053.00	737.2
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.64]	kPa	[258.23; 378.22]	The Yaw...
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.38484e+01
Coefficient B			-2.76500e+03
Coefficient C			-5.43350e+01
Temperature range, min.			258.23
Temperature range, max.			378.22
Pvap	1.33	kPa	258.23	Calculated Property
Pvap	3.06	kPa	271.56	Calculated Property
Pvap	6.40	kPa	284.89	Calculated Property
Pvap	12.32	kPa	298.23	Calculated Property
Pvap	22.18	kPa	311.56	Calculated Property
Pvap	37.66	kPa	324.89	Calculated Property
Pvap	60.86	kPa	338.22	Calculated Property
Pvap	94.21	kPa	351.56	Calculated Property
Pvap	140.46	kPa	364.89	Calculated Property
Pvap	202.64	kPa	378.22	Calculated Property
Pvap	[5.32; 4077.96]	kPa	[279.69; 553.54]	KDB Vap...
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			7.56506e+01
Coefficient B			-6.35490e+03
Coefficient C			-9.20098e+00
Coefficient D			7.37481e-06
Temperature range, min.			279.69
Temperature range, max.			553.54
Pvap	5.32	kPa	279.69	Calculated Property
Pvap	21.81	kPa	310.12	Calculated Property
Pvap	66.56	kPa	340.55	Calculated Property
Pvap	164.18	kPa	370.97	Calculated Property
Pvap	346.38	kPa	401.40	Calculated Property
Pvap	650.51	kPa	431.83	Calculated Property
Pvap	1119.43	kPa	462.26	Calculated Property
Pvap	1803.27	kPa	492.68	Calculated Property
Pvap	2763.29	kPa	523.11	Calculated Property
Pvap	4077.96	kPa	553.54	Calculated Property

Similar Compounds

Find more compounds similar to Cyclohexane.

Mixtures

• n-Hexane + Cyclohexane
• 1,3-Dioxolane + Cyclohexane
• 1,4-Dioxane + Cyclohexane
• 1-Butanol + Cyclohexane
• Benzene + 1-Propanol + Cyclohexane
• Acetic acid, butyl ester + Cyclohexane
• Cyclohexanone + Cyclohexane
• n-Butyl ether + Cyclohexane
• Toluene + Cyclohexane
• Toluene + n-Butyl ether + Cyclohexane
• 2,3-Pentanedione + Cyclohexane
• Butane, 1-chloro- + Cyclohexane
• Butane, 2-chloro- + Cyclohexane
• Ethanol, 2-ethoxy- + Cyclohexane
• Cyclohexane + Ethane, 1,1,2,2-tetrachloro-
• Diethyl sulfide + Cyclohexane
• Benzene + Cyclohexane
• 2-Pyrrolidinone, 1-methyl- + Cyclohexane
• Acetone + Cyclohexane
• Diisopropyl ether + Cyclohexane

Find more mixtures with Cyclohexane.

Sources

• KDB Pure (Korean Thermophysical Properties Databank)
• KDB Vapor Pressure Data
• Crippen Method
• Dortmund Data Bank Vapor-Liquid Equilibrium Data
• Densities, Viscosities, and Refractive Indices of Mixtures of Hexane with Cyclohexane, Decane, Hexadecane, and Squalane at 298.15K
• Speeds of Sound and Isentropic Compressibilities for Binary Mixtures of a Cyclic Diether with a Cyclic Compound at Three Temperatures
• Acoustic and Thermophysical Properties of Binary Liquid Mixtures of Primary Butanols with Hexane and Cyclohexane at 293.15 K
• Densities and Kinematic Viscosities of One Quinary Regular Liquid System and Its Five Quaternary Sub-Systems at Temperatures (293.15 and 298.15) K
• Densities and Kinematic Viscosities of a Quinary Regular Liquid System and Its Five Quaternary Subsystems at 293.15A K and 298.15A K
• Fluid Phase Topology of Benzene + Cyclohexane + 1-Propanol at 101.3 kPa
• Hydrogen solubility in a chemical hydrogen storage medium, aromatic hydrocarbon, cyclic hydrocarbon, and their mixture for fuel cell systems
• Experimental solubility data of various n-alkane waxes: effects of alkane chain length, alkane odd versus even carbon number structures, and solvent chemistry on solubility
• Determination of activity coefficients at infinite dilution of organic solutes in the ionic liquid, trihexyl(tetradecyl)-phosphonium tris(pentafluoroethyl) trifluorophosphate, by gas liquid chromatography
• Topological and thermodynamic investigations of molecular interactions in binary mixtures: Molar excess volumes and molar excess enthalpies
• Activity coefficients in binary mixtures formed by cyclohexanone with a variety of compounds at 94.7 kPa
• Isobaric vapor liquid and vapor liquid liquid equilibrium data for the system water + ethanol + cyclohexane
• Vapour liquid equilibrium of carboxylic acid systems: Propionic acid + valeric acid and isobutyric acid + valeric acid
• Experimental and predicted vapour liquid equilibrium of 1,4-dioxane with cycloalkanes and benzene
• Experimental liquid liquid equilibria of 1-methylimidazole with hydrocarbons and ethers
• Deuterium isotope effects in liquid liquid phase diagrams of aniline + cyclohexane mixtures
• Experimental investigation of the vapour-liquid equilibrium of binary and ternary mixtures containing dibutyl ether (DBE), cyclohexane and toluene at 313.15 K
• Isobaric vapor liquid equilibria for ethanol water system containing different ionic liquids at atmospheric pressure
• Phase diagrams of binary systems containing n-alkanes, or cyclohexane, or 1-alkanols and 2,3-pentanedione at atmospheric and high pressure
• Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
• Determination of activity coefficients at infinite dilution of organic solutes in the ionic liquid, tributylmethylphosphonium methylsulphate by gas liquid chromatography
• Experimental and predicted excess molar enthalpies for 1,4-dioxane + octane + cyclohexane at 303.15 K
• Excess enthalpies of binary mixtures of 2-ethoxyethanol with four hydrocarbons at 298.15, 308.15, and 318.15K An experimental and theoretical study
• Phase behaviour of I-hexyloxymethyl-3-methyl-imidazolium and 1,3-dihexyloxymethyl-imidazolium based ionic liquids with alcohols, water, ketones and hydrocarbons: The effect of cation and anion on solubility
• Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent
• Thermodynamic study of 1,1,2,2-tetrachloroethane + hydrocarbon mixtures I. Excess and solvation enthalpies
• Vapor liquid equilibrium for binary system of diethyl sulfide + cyclohexane at 353.15 and 343.15 K and diethyl sulfide + 2-ethoxy-2-methylpropane at 343.15 and 333.15 K
• Determination and correlation of vapor liquid equilibrium for binary systems consisting of close-boiling components
• Liquid liquid equilibrium of ternary systems containing nicotine
• Determination and correlation of liquid liquid equilibria for four binary N,N-dimethylformamide + hydrocarbon systems
• Solubility of naproxen in several organic solvents at different temperatures
• Hydrogen solubility of mixed naphthenes and aromatics for a new hydrogen storage medium in fuel cell system
• Liquid liquid equilibria of lactam containing binary systems
• Vapor liquid equilibria and interfacial tensions for the ternary system acetone + 2,2 -oxybis[propane] + cyclohexane and its constituent binary systems
• Phase equilibria and interfacial tensions in the systems methyl tert-butyl ether + acetone + cyclohexane, methyl tert-butyl ether + acetone and methyl tert-butyl ether + cyclohexane
• Solubility of hydrocarbons in water: Experimental measurements and modeling using a group contribution with association equation of state (GCA-EoS)
• Measurement and correlation of vapor pressure of benzene and thiophene with BMIM][PF6] and [BMIM][BF4] ionic liquids
• 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
• Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium trifluoromethanesulfonate using GLC
• Phase equilibria on four binary systems containing 3-methylthiophene
• 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
• Liquid phase equilibria for mixtures of (an aliphatic hydrocarbon + toluene + gamma-butyrolactone)
• (Liquid + liquid) equilibria of the quaternary sysytem methanol + isooctane + cyclohexane + benzene at T = 303.15 K
• Experimental solid-liquid phase equilibria of {cholesterol + binary solvent mixture: 1-Alcohol (C4-C10) + cyclohexane}
• Thermodynamic analysis of the solubility of ketoprofen in some propylene glycol + water cosolvent mixtures
• Isobaric vapor-liquid equilibria for binary and ternary mixtures with cyclohexane, cyclohexene, and morpholine at 100 kPa
• Liquid-liquid equilibria for ternary systems of {cyclohexane + aromatic compounds + 1-ethyl-3-methylpyridinium ethylsulfate}
• Measurements of binary diffusion coefficients for metal complexes in organic solvents by the Taylor dispersion method
• Excess Gibbs energies and volumes of the ternary system chloroform + tetrahydrofuran + cyclohexane at 298.15 K
• "Vapor-liquid" equilibrium measurements and modeling for the cyclohexane + cyclohexanol binary system
• Solubility of benzoic acid in acetone, 2-propanol, acetic acid and cyclohexane: Experimental measurement and thermodynamic modeling
• Gas-liquid chromatography measurements of activity coefficients at infinite dilution of hydrocarbons and alkanols in 1-alkyl-3-methylimidazolium bis(oxalato)borate
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
• Volumetric behavior of the binary systems benzene + cyclohexane and benzene + 2,2,4-trimethyl-pentane at temperatures 293.15-323.15K
• Application of [EMim][ESO4] ionic liquid as solvent in the extraction of toluene from cycloalkanes: Study of liquid-liquid equilibria at T = 298.15 K
• Influence of anion structure on the liquid-liquid equilibria of 1-(3-hydroxypropyl)pyridinium cation based ionic liquid-hydrocarbon binary systems
• Solubility of decanedioic acid in binary solvent mixtures
• Vapor-liquid equilibrium measurements and modeling for the cyclohexane + n-hexanoic acid binary system
• Vapor liquid liquid equilibrium and vapor liquid equilibrium for the quaternary system water ethanol cyclohexane toluene and the ternary system water cyclohexane toluene. Isobaric experimental determination at 101.3 kPa
• Introduction of the amine group at cycloaliphatic hydrocarbon (c-CHNH2) for the modified UNIFAC (Dortmund) model and validation in multicomponent systems containing cyclohexylamine
• Solubility of elemental sulfur in pure organic solvents and organic solvent-ionic liquid mixtures from 293.15 to 353.15 K
• Isobaric vapor-liquid equilibrium for the binary mixtures of nonane with cyclohexane, toluene, m-xylene, or p-xylene at 101.3 kPa
• Ether + alcohol + hydrocarbon mixtures in fuels and bio-fuels: Excess enthalpies of binary mixtures containing dibutyl ether (DBE) or 1-butanol and 1-hexene or methylcyclohexane or toluene or cyclohexane or 2,2,4-trimethylpentane at 298.15K and 313.15K
• Capacity of ionic liquids [EMim][NTf2] and [EMpy][NTf2] for extraction of toluene from mixtures with alkanes: Comparative study of the effect of the cation
• Thermodynamic characterization of second generation biofuels: Vapour-liquid equilibria and excess enthalpies of the binary mixtures 1-pentanol and cyclohexane or toluene
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid ethyl(2-hydroxyethyl)dimethyl-ammonium diethylphosphate using gas liquid chromatography
• Activity coefficients at infinite dilution of organic solutes in 1-octyl-3-methylimidazolium nitrate using gas-liquid chromatography
• Effect of 1-methyl 3-octylimidazolium thiocyanate on vapor-liquid equilibria of binary mixtures of hydrocarbons
• Isobaric vapor-liquid-liquid equilibrium for water + cyclohexane + acetic acid at 101.3 kPa
• Using binary mixtures of dicationic ionic liquids for determination ofactivity coefficients at infinite dilution by gas-liquid chromatography
• A novel dynamic recirculating apparatus for vapour-liquid equilibrium measurements at moderate pressures and temperatures
• Phase equilibria and excess molar enthalpies study of the binary systems (pyrrole + hydrocarbon, or an alcohol) and modeling
• Experimental data, correlation and prediction of the extraction of benzene from cyclic hydrocarbons using [Epy][ESO4] ionic liquid
• Measurements of activity coefficients at infinite dilution in vegetable oils and capric acid using the dilutor technique
• Towards automated characterisation of liquid-liquid equilibria
• Volumetric investigation of the ternary system ethanol + dimethylformamide + cyclohexane at 298.15 K
• VLE and LLE in ternary systems of two associating components (water, aniline, and cyclohexylamine) and a hydrocarbon (cyclohexane or methylcyclohexane)
• Miscibility behavior of trihexyl(tetradecyl)phosphonium tetrafluoroborate with cyclic hydrocarbons
• Isothermal vapour pressures and thermodynamic excess properties of 3,5- and 2,6-dimethylpyridine with cyclohexane. Measurements and prediction
• Thermodynamic properties of cyclohexane methanol liquid mixture from shear viscosity measurements
• Study of interaction between organic compounds and mono or dicationic oxygenated ionic liquids using gas chromatography
• The role of organic diluents in the aspects of equilibrium, kinetics and thermodynamic model for silver ion extraction using an extractant D2EHPA
• Distribution of cyclohexanol and cyclohexanone between water and cyclohexane
• Determination and correlation of solubility and solution thermodynamics of coumarin in different pure solvents
• Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
• Mesoscale solubilization and critical phenomena in binary and quasi-binary solutions of hydrotropes
• Thermodynamics properties, VLE and HE, of the systems 2-pentanol and cyclohexane or methylbenzene for contributing to the knowledge of new biofuels
• Measurement and correlation of solid-liquid equilibria for three binaries, ethanol-antipyrine, chloroform-antipyrine, and dimethyl ether-antipyrine
• Solubilities of adipic acid in binary cyclohexanone + cyclohexanol, cyclohexane + cyclohexanol, and cyclohexane + cyclohexanone solvent mixtures
• 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
• Separation of hex-1-ene/hexane and cyclohexene/cyclohexane compounds with [EMIM]-based ionic liquids
• Measurement and prediction of liquid-liquid equilibria in ternary systems containing water, an organic component, and cyclohexanol
• In situ measurement of liquid-liquid equilibria by medium field nuclear magnetic resonance
• High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
• Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
• Measurements of activity coefficient at infinite dilution for organic solutes in tetramethylammonium chloride + ethylene glycol deep eutectic solvent using gas-liquid chromatography
• Ternary LLE measurements for the separation of hex-1-ene/hexane and cyclohexene/cyclohexane compounds with [DCA]-based ionic liquids
• Plotting of phase (vapor-liquid) transition surface near the critical point out of data from isochoric experiment. Experimental procedure
• Quaternary isothermal vapor-liquid equilibrium of the model biofuel 2-butanone + n-heptane + tetrahydrofuran + cyclohexane using Raman spectroscopic characterization
• Measurement of critical properties for binary and ternary mixtures containing potential gasoline additive diethyl carbonate (DEC)
• Tetramethylammonium chloride + glycerol deep eutectic solvent as separation agent for organic liquid mixtures: Assessment from experimental limiting activity coefficients
• Vapor-liquid equilibrium in the binary and ternary systems containing ethyl propionate, ethanol and alkane at 101.3 kPa
• New ionic liquid [P4,4,4,4][NTf2] in bio-butanol extraction on investigation of limiting activity coefficients
• Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
• Phase equilibria of 1-hexyl-3-methylimidazolium acetate with water and oil
• Measurements of activity coefficients at infinite dilution for organic solutes in two quaternary ammonium-based ionic liquids [DDA][ClO4] and [DDA][BF4]
• Study of molecular interactions and preferential solvation in binary mixtures of cyclohexane and (C5-C10) 1-alkanol by Kirkwood-Buff integrals
• Application of trihexyltetradecylphosphonium dicyanamide ionic liquid for various types of separations problems: Activity coefficients at infinite dilution measurements utilizing GLC method
• Solubility measurements and thermodynamic modeling of pyrazinamide in five different solvent-antisolvent mixtures
• 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.
• Excess molar enthalpies of the ternary mixtures: (methyl tert-butyl ether or 2-methyltetrahydrofuran + cyclohexane + 2,2,4- trimethylpentane} at the temperature 298.15 K
• 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 + liquid equilibria for ternary mixtures of (solvent + aromatic hydrocarbon + alkane)
• Excess molar volumes of the ternary system {methylcyclohexane (1) + cyclohexane (2) + n-alkanes (3)} at T = 298.15 K
• Partial molar volume of paracetamol in water, 0.1 M HCl and 0.154 M NaCl at T = (298.15, 303.15, 308.15 and 310.65) K and at 101.325 kPa
• 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)
• 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
• Thermophysical study of 1,4-dioxane with cycloalkane mixtures
• Azeotropic behaviour of (benzene + cyclohexane + chlorobenzene) ternary mixture using chlorobenzene as entrainer at 101.3 kPa
• Thermodynamic properties of binary mixtures of N-methyl-2-pyrrolidinone with cyclohexane, benzene, toluene at (303.15 to 353.15) K and atmospheric pressure
• Dynamic viscosities of binary mixtures of cycloalkanes with primary alcohols at T = (293.15, 298.15, and 303.15) K: New UNIFAC-VISCO interaction parameters
• Measurement of activity coefficients at infinite dilution in 1-hexadecyl-3-methylimidazolium tetrafluoroborate ionic liquid
• Mixing properties of binary mixtures presenting azeotropes at several temperatures
• Thermodynamic study of (perfluoroalkane + alkane) mixtures: Excess and solvation enthalpies
• (p,Vm,T) measurements of (cyclohexane + nonane) at temperatures from 298.15 K to 328.15 K and at pressures up to 40 MPa
• (Liquid + liquid) equilibria of [C8mim][NTf2] ionic liquid with a sulfur-component and hydrocarbons
• Densities, viscosities, and excess properties of (N-methylmorpholine + cyclohexane, + benzene, and + toluene) at T = (298.15, 303.15, 313.15, 323.15) K
• Measurements of activity coefficients at infinite dilution of aromatic and aliphatic hydrocarbons, alcohols, and water in the new ionic liquid [EMIM][SCN] using GLC
• Measurement and correlation of (liquid + liquid) equilibrium of the azeotrope (cyclohexane + 2-butanone) with different ionic liquids at T = 298.15 K
• 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
• Evaluation of (vapor + liquid) equilibria for the binary systems (1-octanol + cyclohexane) and (1-octanol + n-hexane), at low alcohol compositions
• Thermodynamics of biofuels: Excess enthalpies for binary mixtures involving ethyl 1,1-dimethylethyl ether and hydrocarbons at different temperatures using a new flow calorimeter
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid triethylsulphonium bis(trifluoromethylsulfonyl)imide
• Measurements of activity coefficients at infinite dilution of aliphatic and aromatic hydrocarbons, alcohols, thiophene, tetrahydrofuran, MTBE, and water in ionic liquid [BMIM][SCN] using GLC
• 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
• Activity coefficients at infinite dilution for solutes in the trioctylmethylammonium bis(trifluoromethylsulfonyl)imide ionic liquid using gas liquid chromatography
• (Liquid + liquid) equilibria for ternary mixtures of (water + propionic acid + organic solvent) at T = 303.2 K
• (Liquid + liquid) equilibria of (heptane, or hexane, or cyclohexane + toluene + 1,3- dimethyl-2-imidazolidinone) ternary systems at T = 298.15 K
• 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
• (Liquid + liquid) equilibria in ternary aqueous mixtures of phosphoric acid with organic solvents at T = 298.2 K
• Gas liquid chromatography measurements of activity coefficients at infinite dilution of various organic solutes and water in tri-iso-butylmethylphosphonium tosylate ionic liquid
• Excess properties and vapour pressure of {3-diethylaminopropylamine + cyclohexane}
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate [EMIM][TCB] using gas liquid chromatography
• (Vapour + liquid) equilibria of ternary systems with ionic liquids using headspace gas chromatography
• A thermodynamic study on solubility and liquid-liquid phase behaviour for 2,2,2-trifluoroethanol + cyclohexane + 1-butanol at three temperatures and pressure 101.3 kPa
• Measurements of activity coefficients at infinite dilution of organic solutes and water in 1-propyl-1-methylpiperidinium bis{(trifluoromethyl)sulfonyl}imide ionic liquid using g.l.c.
• Activity coefficients at infinite dilution of organic solutes in N-alkylpyridinium bis(trifluoromethylsulfonyl)imide ([CnPY][NTf2], n = 2, 4, 5) using gas liquid chromatography
• Measurement and correlation of the (p, rho, T) relation of liquid cyclohexane, toluene, and ethanol in the temperature range from 233.15 K to 473.15 K at pressures up to 30 MPa for use as density reference liquids
• (Liquid + liquid) equilibria for mixtures of (ethylene glycol + benzene + cyclohexane) at temperatures (298.15, 308.15, and 318.15) K
• Measurements of activity coefficients at infinite dilution of organic compounds and water in isoquinolinium-based ionic liquid [C8iQuin][NTf2] using GLC
• Thermodynamic properties of chiral fenchones in some solutions at T = 298.15 K
• 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
• Separation of toluene from cyclic hydrocarbons using 1-butyl-3-methylimidazolium methylsulfate ionic liquid at T = 298.15 K and atmospheric pressure
• (Liquid + liquid) equilibrium data for the ternary systems (cycloalkane + ethylbenzene + 1-ethyl-3-methylimidazolium ethylsulfate) at T = 298.15 K and atmospheric pressure
• Thermodynamic and topological investigations of molecular interactions in binary and ternary mixtures containing 1-methyl pyrrolidin-2-one at T = 308.15 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
• Measurement of (liquid + liquid) equilibria for ternary systems of (N-formylmorpholine + benzene + cyclohexane) at temperatures (303.15, 308.15, and 313.15) K
• Compressed liquid density measurements for {methylbenzoate + (cyclohexane or 1-hexanol)} binary systems
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
• Quaternary isobaric (vapor + liquid + liquid) equilibrium and (vapor + liquid) equilibrium for the system (water + ethanol + cyclohexane + heptane) at 101.3 kPa
• 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
• Interactions of volatile organic compounds with the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
• Solubilities of some organic solutes in 1-ethyl-3-methylimidazolium acetate. Chromatographic measurements and predictions from COSMO-RS
• 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
• (Liquid + liquid) equilibria for the ternary mixtures (alkane + toluene + ionic liquid) at T = 298.15 K: Influence of the anion on the phase equilibria
• Evaluation of the ionic liquids 1-alkyl-3-methylimidazolium hexafluorophosphate as a solvent for the extraction of benzene from cyclohexane: (Liquid + liquid) equilibria
• 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
• (Liquid + liquid) equilibria of {benzene + cyclohexane + two ionic liquids} at different temperature and atmospheric pressure
• 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
• Experimental study on vapor-liquid equilibria of ternary systems of hydrocarbons/ionic liquid using headspace gas chromatography
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
• 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
• Application of [HMim][NTf2], [HMim][TfO] and [BMim][TfO] ionic liquids on the extraction of toluene from alkanes: Effect of the anion and the alkyl chain length of the cation on the LLE
• 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 coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds: Saturated fatty acids
• Excess properties and vapour pressure of 2-diethylaminoethylamine + cyclohexane
• Thermodynamics of mixtures containing amines. XI. Liquid + liquid equilibria and molar excess enthalpies at 298.15 K for N-methylaniline + hydrocarbon systems. Characterization in terms of DISQUAC and ERAS models
• Heat capacities and densities of the binary mixtures containing ethanol, cyclohexane or 1-hexene at high pressures
• 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
• Volumetric and acoustic properties of binary mixtures of tri-n-butyl phosphate with n-hexane, cyclohexane, and n-heptane from T = (298.15 to 323.15) K
• Interactions of volatile organic compounds with the ionic liquids 1-butyl-1-methylpyrrolidinium tetracyanoborate and 1-butyl-1-methylpyrrolidinium bis(oxalato)borate
• Physicochemical properties and activity coefficients at infinite dilution for organic solutes and water in a novel bicyclic guanidinium superbase-derived protic ionic liquid
• Isothermal (vapour + liquid) equilibria for binary mixtures of diisopropyl ether with (methanol, or ethanol, or 1-butanol): Experimental data, correlations, and predictions
• Solubilities of evodiamine in twelve organic solvents from T = (283.2 to 323.2) K
• Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds Part II: C18 fatty acids
• 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
• Measurements of activity coefficients at infinite dilution for organic solutes and water in N-hexylisoquinolinium thiocyanate, [HiQuin][SCN] using GLC
• Activity coefficients at infinite dilution of organic solutes in N-formylmorpholine and N-methylpyrrolidone from gas-liquid chromatography
• Measurement of critical temperatures and critical pressures for binary mixtures of methyl tert-butyl ether (MTBE) + alcohol and MTBE + alkane
• Phase equilibria study of the (N-octylisoquinolinium thiocyanate ionic liquid + aliphatic and aromatic hydrocarbon, or thiophene) binary systems
• 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
• Infinite dilution activity coefficients of volatile organic compounds in two ionic liquids composed of the tris(pentafluoroethyl) trifluorophosphate ([FAP]) anion and a functionalized cation
• 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
• The study of activity coefficients at infinite dilution for organic solutes and water in 1-butyl-4-methylpyridinium dicyanamide, [B4MPy][DCA] using GLC
• 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
• Activity coefficients at infinite dilution of organic solutes in 1-hexyl-3- methylimidazolium trifluoroacetate and influence of interfacial adsorption using gas liquid chromatography
• Contribution to study of the thermodynamics properties of mixtures containing 2-methoxy-2-methylpropane, alkanol, alkane
• Densities, viscosities, and isobaric heat capacities of the system (1-butanol + cyclohexane) at high pressures
• Quaternary (liquid + liquid) equilibrium data for the extraction of toluene from alkanes using the ionic liquid [EMim][MSO4]
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-butyl-3-methylimidazolium methyl sulfate
• Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
• Excess enthalpy for the (benzene + cyclohexane) mixture over a wide range of temperature and pressure
• Thermodynamics of solvation in propylene glycol and methyl cellosolve
• Excess molar volumes and excess isentropic compressibilities of binary and ternary mixtures of o-chlorotoluene with cyclic ether and amides or cyclohexane at different temperatures
• Pressure dependence of excess enthalpy for (benzene + cyclohexane) mixture near the critical locus at T = (558.2, 563.2 and 573.2) K and p = (3 to 15) MPa
• (Liquid + liquid) equilibria for (benzene + cyclohexane + dimethyl sulfoxide) system at T = (298.15 or 303.15) K: Experimental data and correlation
• Solvation parameter model and thermodynamic parameters in a dicationic ionic liquid based on pyrrolidinium
• Experimental and theoretically study of interaction between organic compounds and tricyanomethanide based ionic liquids
• Measurements and modeling of LLE and HE for (methanol + 2,4,4-trimethyl-1-pentene), and LLE for (water + methanol + 2,4,4-trimethyl-1-pentene)
• Activity coefficients at infinite dilution of organic solutes in methylphosphonate based ionic liquids using gas-liquid chromatography
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(3-hydroxypropyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
• Volumetric, acoustic, and refractometric properties of (thiophene + hexane/cyclohexane) solutions in the presence of some imidazolium based ionic liquids at T = 298.15 K
• Solubility of daidzin in different organic solvents and (ethyl alcohol + water) mixed solvents
• Activity coefficients at infinite dilution for organic solutes and water in 1-ethyl-1-methylpyrrolidinium lactate
• Measurement and correlation of the solubility of genistin in eleven organic solvents from T = (283.2 to 323.2) K
• 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
• (Vapour + liquid) equilibria, (VLE) excess molar enthalpies and infinite dilution activity coefficients of selected binary systems involving n-hexyl pyridinium bis(trifluoromethylsulphonyl)imide ionic liquid: Experimental and predictions using modified UNIFAC (Dortmund)
• The effect of the naphthenic ring on the VLE of (carbon dioxide + alkane) mixtures
• 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
• (Liquid + liquid) equilibrium of ternary and quaternary systems containing heptane, cyclohexane, toluene and the ionic liquid [EMim][N(CN)2]. Experimental data and correlation
• Selective recovery of aliphatics from aromatics in the presence of the {[4empy][Tf2N] + [emim][DCA]} ionic liquid mixture
• A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
• Solubility measurement and thermodynamic functions of dehydroepiandrosterone acetate in different solvents at evaluated temperatures
• Measurement and correlation of solubility of pronamide in five organic solvents at (278.15-323.15) K
• Determination and correlation of solubility and thermodynamic properties of pyraclostrobin in pure and binary solvents
• Experimental determination of critical data of multi-component mixtures containing potential gasoline additives 2-butanol by a flow-type apparatus
• Solubility and solution thermodynamics of 2-methyl-6-nitroaniline in ten organic solvents at elevated temperatures
• Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in 1-allyl-3-methylimidazolium bis{(trifluoromethyl)sulfonyl}imide ionic liquid
• Separation of aliphatic from aromatic hydrocarbons and sulphur compounds from fuel based on measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid N,N-diethyl-N-methyl-N-(2-methoxy-ethyl)ammonium bis(trifluoromethylsulfonyl)imide
• Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-hexyl-2,3-dimethylimidazolium bis(trifluoromethylsulfonyl)imide
• Solubility determination and thermodynamic modeling of 3-methyl-4- nitrobenzoic acid in twelve organic solvents from T = (283.15-318.15) K and mixing properties of solutions
• Solubility determination and thermodynamic modelling of 2,4-dihydro-5-methyl-2-(4-methylphenyl)-3H-pyrazol-3-one in twelve organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
• Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
• Excess enthalpies of ternary mixtures of (oxygenated additives + cycloalkane) in fuels and bio-fuels: (dibutyl ether + 1-propanol + cyclohexane), or methylcyclohexane, at T = (298.15 and 313.15) K
• Activity coefficients at infinite dilution of hydrocarbons in glycols: Experimental data and thermodynamic modeling with the GCA-EoS
• Solubility and solution thermodynamics of 2-methyl-4-nitroaniline in eleven organic solvents at elevated temperatures
• Solubility measurement and thermodynamic functions of 3-nitrobenzaldehyde in different solvents at elevated temperatures
• Bis(trifluoromethylsulfonyl)imide, or dicyanamide-based ionic liquids in the liquid liquid extraction of hex-1-ene from hexane and cyclohexene from cyclohexane
• Liquid-liquid separation of hex-1-ene from hexane and cyclohexene from cyclohexane with ionic liquids
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
• Solubility modelling and dissolution properties of 5-phenyltetrazole in thirteen mono-solvents and liquid mixtures of (methanol + ethyl acetate) at elevated temperatures
• Thermophysical approach to understand the nature of molecular interactions and structural factor between methyl isobutyl ketone and organic solvents mixtures
• Thermodynamics and activity coefficients at infinite dilution for organic compounds and water in the ionic liquid 1-butyl-3-methylimidazolium perchlorate
• Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
• Liquid-liquid separation of hexane/hex-1-ene and cyclohexane/cyclohexene by dicyanamide-based ionic liquids
• 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 hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on gamma infinity data measurements
• Separation of binary mixtures based on gamma infinity data using [OMMIM][NTf2] ionic liquid and modelling of thermodynamic functions
• The contour of excess molar enthalpy at a mole fraction of benzene x = 0.548 on the p-T plane in liquid state and near the critical points for the (benzene + cyclohexane) mixture
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid trihexyl-tetradecyl-phosphonium tricyanomethanide
• Thermodynamic study of molecular interaction-selectivity in separation processes based on limiting activity coefficients
• Abraham model correlations for describing the thermodynamic properties of solute transfer into pentyl acetate based on headspace chromatographic and solubility measurements
• Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in ionic liquid [HMMIM][BF4]
• Determination of thermophysical properties of cyclopentane hydrate using a stirred calorimetric cell
• The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
• Thermodynamics and activity coefficients at infinite dilution for organic compounds in the ionic liquid 1-hexyl-3-methylimidazolium chloride
• Separation of binary mixtures based on gamma infinity data using [OMMIM][BF4] ionic liquid and modelling of thermodynamic functions
• Determination of the thermodynamic parameters of ionic liquid 1-propyl-3-methylimidazolium bromide by gas-liquid chromatography
• Imidazolium and pyridinium-based ionic liquids for the cyclohexane/cyclohexene separation by liquid-liquid extraction
• Equilibrium solubility of dinitolmide in several neat solvents and binary aqueous co-solvent mixtures: Experimental determination and thermodynamic analysis
• Isobaric vapor-liquid equilibrium of three binary systems containing dimethyl succinate, dimethyl glutarate and dimethyl adipate at 2, 5.2 and 8.3 kPa
• Determination and correlation of solubility and solution thermodynamics of musk xylene in different pure solvents
• Densities, isobaric thermal compressibilities and derived thermodynamic properties of the binary systems of cyclohexane with allyl methacrylate, butyl methacrylate, methacrylic acid, and vinyl acetate at t = (298.15 and 308.15)K
• Volumetric and viscometric studies of molecular interaction of the ternary system toluene (1) + cyclohexane (2) + n-hexane (3) at 298.15K
• Studies of partial molar volumes of alkylamine in non-electrolyte solvents I. Alkylamines in hydrocarbons at 303.15 and 313.15K
• Excess volumes, densities, speeds of sound and viscosities for the binary systems of diisopropyl ether with hydrocarbons at 303.15K
• Liquid liquid equilibria for mixtures of (ethylene carbonate + aromatic hydrocarbon + cyclohexane)
• Thermophysical properties and thermodynamic phase behavior of ionic liquids
• Topological and thermodynamic investigations of binary mixtures: Molar excess volumes, molar excess enthalpies and isentropic compressibility changes of mixing
• Volumetric and transport properties of ternary mixtures containing 1-propanol, triethylamine or tri-n-butylamine and cyclohexane at 303.15 K: Experimental data, correlation and prediction by ERAS model
• Volumetric and transport properties of ternary mixtures containing 1-propanol + ethyl ethanoate + cyclohexane or benzene at 303.15 K: Experimental data, correlation and prediction by ERAS model
• Volumetric and transport properties of ternary mixtures containing 1-alkanol + ethyl ethanoate + cyclohexane at 303.15 K: Experimental data, correlation and prediction by ERAS model
• Excess molar volumes and isentropic compressibilities changes of mixing of tetrahydropyran + benzene + cyclo or n-alkanes ternary mixtures at 308.15 K
• Thermodynamic properties of binary mixtures containing Tetrahydropyran: Excess molar volumes, Excess molar enthalpies and isentropic compressibilities changes of mixing
• THERMODYNAMICS OF MIXTURES CONTAINING ALKOXYETHANOLS. XXVIII. LIQUID-LIQUID EQUILIBRIA FOR 2-PHENOXYETHANOL + SELECTED ALKANES
• Phase diagrams for the aqueous solutions of butyric acid with cyclohexane at different temperatures: Experimental and correlated data
• Volumetric and Acoustic Properties of Binary Mixtures of Cyclohexane + Benzene and + Benzaldehyde at (293.15 to 323.15) K
• Temperature dependence of densities, speeds of sound, and derived properties of cyclohexylamine + cyclohexane or benzene in the range (293.15 to 323.15) K
• Development of a certified reference material for calibration of DSC and DTA below room temperature: NMIJ CRM 5401-a, Cyclohexane for Thermal Analysis
• A new analysis method for improving collection of vapor-liquid equilibrium (VLE) data of binary mixtures using differential scanning calorimetry (DSC)
• Vapor Liquid Equilibrium Data for Binary Systems of N,N-Dimethylacetamide with Cyclohexene, Cyclohexane, and Benzene Separately at Atmospheric Pressure
• Viscous Calibration Liquids for Self-diffusion Measurements
• Viscosities of liquid cyclohexane and decane at temperatures between (303 and 598) K and pressures up to 4 MPa measured in a dual-capillary viscometer
• Excess Molar Volumes for Three and Four Component Mixtures Simulating the Binary Mixture (Cyclohexane+ Hexadecane)
• Isobaric Vapor Liquid Liquid Equilibrium for Water + Cyclohexane + Acrylic Acid at 200 mmHg
• Solubilities of 3-Chlorophthalic Anhydride and 4-Chlorophthalic Anhydride in Different Pure Solvents
• Liquid Liquid Equilibrium data for the ternary systems of Water, Isopropyl alcohol, and selected entrainers
• Solubility and Dissolution Thermodynamics for 1,3,5- Trichlorobenzene in Organic Solvents
• Experimental and Computational Study on Liquid Liquid Equilibrium in Ternary Systems of -Valerolactone, Toluene, and Hydrocarbons
• Solubility Determination and Modeling of Sodium Mononitrobenzenesulphonate in Different Solvents at Temperatures Ranging from (283.15 to 323.15) K
• Solubilities of Adipic Acid in Cyclohexanol + Cyclohexanone Mixtures and Cyclohexanone + Cyclohexane Mixtures
• Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
• Vapor Liquid Equilibria for (n-Hexane, n-Octane, Cyclohexane, or 2,3-Dimethylpentane) + Toluene + {[4empy][Tf2N] (0.3) + [emim][DCA] (0.7)} Mixed Ionic Liquids
• Design of Equilibrium Cells for Phase Equilibria and PVT Measurements in Large Ranges of Temperatures and Pressures. I. Vapor Liquid Liquid Equilibria
• Determination and Correlation for the Solubility of Glutaric Acid in Cyclohexane + Cyclohexanol + Cyclohexanone Solvent Mixtures
• Solubility of 2-Ethylanthraquinone in Binary Mixtures of Oligooxymethylene Dimethyl Ethers with Different Number of CH2O Groups of n = 2, 3, and 4 from 293.15 to 343.15 K
• Solubility of 4-Methylsulfonylacetophenone in Nine Pure Solvents and (Ethyl Acetate + n-Hexane) Binary Solvent Mixtures from 278.15 K to 328.15 K
• Measurement and Correlation of Solubility of Amorphous Cefmetazole Sodium in Pure Solvents and Binary Solvent Mixtures
• Measurement and Correlation of the Solubility of e-CL-20 in 12 Organic Solvents at Temperatures Ranging from 278.15 to 318.15 K
• Measurement and Prediction of Vapor Liquid(-Liquid) Equilibria in Ternary Systems Containing Water, an Organic Component, and Cyclohexanol
• Influence of Temperature on the Liquid Liquid Phase Equilibria of Ternary (Water + Alcohol + Entrainer) Systems
• The Critical Temperatures of a Number of (i) (Chloroalkane (C3 C4) + Hydrocarbon (C6 C7)) Binary Mixtures and (ii) (Aromatic Halocarbon (Chlorobenzene, Fluorobenzene, 1,2-Dichlorobenzene, or 1,3-Dichlorobenzene) + Alkane (C8)) Binary Mixtures
• Determination of Infinite Dilution Activity Coefficients of Several Organic Solutes in N-Butylpyridinium Nitrate/N-Octylpyridinium Nitrate by Blend Inverse Gas Chromatography
• Extraction of Low Concentration Aqueous Solution of Methylal: Liquid Liquid Equilibrium in Water + Methylal + (Cyclohexane and n-Heptane) Ternary Systems
• Thermodynamic Functions for the Solubility of 3-Nitrobenzonitrile in 12 Organic Solvents from T/K = (278.15 to 318.15)
• Solubility Measurement and Correlation of Fosfomycin Sodium in Six Organic Solvents and Different Binary Solvents at Temperatures between 283.15 and 323.15 K
• Measurement and Correlation of the Solubilities of Sulfur S8 in 10 Solvents
• Measurement and Prediction of Vapor-Liquid Equilibria in Ternary Systems Containing an Organic Component, Cyclohexylamine, and Cyclohexanol
• Solubility Modeling and Mixing Properties for Benzoin in Different Monosolvents and Solvent Mixtures at the Temperature Range from 273.15 to 313.15 K
• Measurement and Correlation of the Dissolution Equilibria of o-Iodoaniline and p-Iodoaniline in Pure Solvents
• Mutual Solubilities of Cyclohexane and Water in Aqueous Methyldiethanolamine /Cyclohexane Liquid-Liquid Equilibria
• Determination and Correlation for the Solubilities of Succinic Acid in Cyclohexanol + Cyclohexanone + Cyclohexane Solvent Mixtures
• Densities and Dynamic Viscosities of Alicyclic Cyclohexane with Toluene, o-Xylene, and Mesitylene at T = (303.15 to 323.15) K and Atmospheric Pressure
• 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
• Measurement and Correlation of the Solubility of Pyrimethanil in Seven Monosolvents and Two Different Binary Mixed Solvents
• Bubble Pressure Measurement and Prediction for n-Hexadecane and n-Eicosane + Cyclohexane, Methylcyclohexane, and Ethylcyclohexane Binary Mixtures from 303.15 to 393.15 K
• Solubility of 2-Chlorophenylacetic Acid in 12 Pure Solvents from T = (273.15/283.15 to 318.15) K: Determination and Modeling
• Solubility Measurement and Modeling of 1-(3-nitrophenyl)Ethanone and 1-(4-nitrophenyl)Ethenone in Nine Pure Organic Solvents from T = (278.15 to 318.15) K and Mixing Properties of Solutions
• Solubility Measurement and Modeling of 2-Amino-4,6-dichoropyrimidine in Ten Pure Solvents and (Ethyl Acetate + Ethanol) Solvent Mixtures
• Solubility Measurement and Correlation for epsilon-2,4,6,8,10,12-Hexanitro-2,4,6,8,10,12-hexaazaisowurtzitane in Different Alkanes/Aromatic Hydrocarbon + Ethyl Acetate Binary Solvents at Temperatures of between 283.15 and 323.15 K
• Solubility Modeling and Solvent Effects of Allopurinol in 15 Neat Solvents
• Solubilities of Organic Semiconductors and Nonsteroidal Anti-inflammatory Drugs in Pure and Mixed Organic Solvents: Measurement and Modeling with Hansen Solubility Parameter
• Activity Coefficients at Infinite Dilution of Various Solutes in Tetrapropylammonium Bromide + 1,6-Hexanediol Deep Eutectic Solvent
• Thermodynamic Parameters of a New Synthesized Tricationic Ionic Liquid Stationary Phase by Inverse Gas Chromatography
• Solubility of Diflufenican in Pure and Binary Solvent Systems
• Determination of Activity Coefficients at Infinite Dilution of Solutes in N,N'-Di(2-ethylhexyl)isobutyramide Using Inverse Gas-Liquid Chromatography
• Measurement and Correlation of Solubility and Thermodynamic Properties of Vinpocetine in Nine Pure Solvents and (Ethanol + Water) Binary Solvent
• Liquid-Liquid-Solid Equilibria in the Ternary System Water-Phosphoric Acid-Cyclohexane at 25 and 35 deg.C: Stability Domain of Hemihydrate and Anhydrous Phosphoric Acid
• Solubility Measurement and Thermodynamic Properties of Levetiracetam in Pure and Mixed Solvents
• Total Pressure Phase Equilibrium Measurements for the Binary Systems of n-Pentane + Cyclohexane and 1-Hexene + 2-Propanol
• A New Test System for Distillation Efficiency Experiments at Elevated Liquid Viscosities: Vapor-Liquid Equilibrium and Liquid Viscosity Data for Cyclopentanol + Cyclohexanol
• Solubility in Different Solvents, Correlation, and Solvent Effect in the Solvent Crystallization Process of Iohexol
• Experimental Mutual Solubility Data for Cyclohexane and Water in Aqueous Solutions of Diethanolamine
• Solubilities of 2,6-Dimethylnaphthalene in Six Pure Solvents and Two Binary Solvent Systems
• Solubility, Model Correlation, and Solvent Effect of 2-Amino-3-methylbenzoic Acid in 12 Pure Solvents
• Solubility Measurement, Correlation, and Molecular Interactions of 3-Methyl-6-nitroindazole in Different Neat Solvents and Mixed Solvents from T = 278.15 to 328.15 K
• Solubility Study of (2E)-1-(3-Pyridyl)-3-(dimethylamino)-2-propen-1-one in Different Pure Solvents and Binary Solvent Mixtures from 278.15 to 328.15 K
• Solubility Determination and Thermodynamic Modeling of 2-Mercaptobenzimidazole in 12 Solvents from T = 278.15 K to T = 318.15 K
• o-Nitrophenylacetonitrile Solubility in Several Pure Solvents: Measurement, Correlation, and Solvent Effect Analysis
• Solubility of Gastrodin in Pure and Mixed Solvents at 273.15-313.15 K and Its Correlation with Different Thermodynamic Models
• Liquid-Liquid Equilibria for Benzene/Thiophene + Cyclohexane/Hexadecane + Deep Eutectic Solvents: Data and Correlation
• Assessment of Pyrrolidinium-Based Ionic Liquid for the Separation of Binary Mixtures Based on Activity Coefficients at Infinite Dilution
• Isothermal Vapor-Liquid Equilibrium Data for the Binary Systems Consisting of 1,1,2,3,3,3-Hexafluoro-1-propene and Either Methylcyclohexane, Cyclohexane, n-Hexane, 2-Methyltetrahydrofuran, or 2,2,3,3,4,4,4-Heptafluoro-1-butanol
• Binary Equilibrium Solubility of Amidinothiourea in Monosolvents: Experimental Determination, Model Correlation, and Solvent Effect Analysis
• Solubility Study and Mixing Property of 3,5-Dinitro-2-methylbenzoic Acid in 13 Pure Solvents from 288.15 to 333.15 K
• Solubility and Solvent Effect of 1-(2-Bromo-phenyl)-pyrrole-2,5-dione in 14 Pure Solvents from 278.15 to 323.15 K
• Determination and Modeling of d-Histidine Solubility in Several Pure Solvents from 293.15 to 333.15 K
• Solubility Determination of 2-Chloronicotinic Acid and Analysis of Solvent Effect
• Solubility measurement and thermodynamic model correlation of sancycline in twelve pure solvents
• Solubility Data for Roflumilast and Maraviroc in Various Solvents between T = (278.2-323.2) K
• Solubility and Solution Thermodynamics of 2,6-Dichloro-4-nitroaniline in 12 Pure Solvents at Temperatures from 278.15 to 323.15 K
• Thermodynamic Properties of Mixtures Containing Precursors of Vitamin B5
• Effect of Composition and Temperature upon Density, Viscosity, Surface Tension, and Refractive Index of 2,2,4-Trimethylpentane + Cyclohexane + Decane Ternary Liquid Systems
• Liquid-Liquid Equilibria for the Binary Systems of N-Formylmorpholine with Cycloalkanes
• Viscosities of Dimethyl Carbonate or Diethyl Carbonate with Alkanes at Four Temperatures. New UNIFAC-VISCO Parameters
• Surface Tension of Pure Liquids and Binary Liquid Mixtures
• Solubility of 1-Alkyl-3-methylimidazolium Hexafluorophosphate in Hydrocarbons
• Bubble Temperature Measurements on Binary Mixtures Formed by Cyclohexane at 94.7 kPa
• Excess Molar Enthalpies for Binary Mixtures of Ethanol + Acetone, + Octane, + Cyclohexane and 1-Propanol + Acetone, + Octane, + Heptane at 323.15
• Excess Enthalpies of the Ternary Mixtures: Tetrahydrofuran + (Hexane or Cyclohexane) + Decane at 298.15K
• Excess Molar Enthalpies for the Binary Systems of Benzene or Cyclohexane with 1,1-Diethoxyethane at 323.15 K or with 2,2-Dimethoxybutane at 303.15 K and Infinite Dilution Activity Coefficients in 1,1-Diethoxyethane
• An apparatus for the on-line GC determination of hydrocarbon solubility in water: benzene and cyclohexane from 70 C to 150 C
• Determination of Isobaric Thermal Expansivity of Organic Compounds from 0.1 to 30 MPa at 30 C with an Isothermal Pressure Scanning Microcalorimeter
• Vapor-Liquid Equilibrium in a Ternary System Cyclohexane + Ethanol + Water
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Hexyl-3-methylimidazolium Hexafluorophosphate from Gas-Liquid Chromatography
• Critical Point Measurements for Five n-Alkylcyclohexanes (C6 to C10) by the Pulse-Heating Method
• Measurement of Activity Coefficients of Solutes at Infinite Dilution in (Dimethyl Sulfoxide + Acetamide, or Formamide, or Urea) Using Gas Liquid Chromatography at the Temperature 298.15 K
• Bubble-Temperature Measurements on Some Binary Mixtures Formed by Tetrahydrofuran or Amyl Alcohol with Hydrocarbons, Chlorohydrocarbons, or Butanols at (94.6 or 95.8) kPa
• Vapor-Liquid Equilibria in Alcohol + Cyclohexane + Water Systems
• Solubility of -Carotene in Binary Solvents Formed by Some Hydrocarbons with Dibutyl Ether and 1,2-Dimethoxyethane
• 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
• Densities, Excess Molar Volumes, Viscosities, Speeds of Sound, Excess Isentropic Compressibilities, and Relative Permittivities for CmH2m+1(OCH2CH2)nOH (m ) 1 or 2 or 4 andn ) 1) + Benzene, + Toluene, + (o-, m-, and p-) Xylenes, + Ethylbenzene, and + Cyclohexane
• Surface Tension and Interfacial Tension of Binary Organic Liquid Mixtures
• Gas-Liquid Critical Temperatures of Some Alkenes, Amines, and Cyclic Hydrocarbons
• Determination and Study on the Solubility of Methane in Heptane + Cyclohexane and Heptane + Ethanol at High Pressures
• Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
• Vapor-Liquid Equilibria of the Binary System 1-Pentanol + Anisole and the Quaternary System Benzene+Cyclohexane+1-Pentanol+Anisole at 101.32 kPa
• Solubility of a-Carotene in Binary Solvents Formed by Some Hydrocarbons with tert-Butyl Methyl Ether and with tert-Amyl Methyl Ether
• Phase Equilibria for the Ternary Liquid Systems of (Water + Tetrahydrofurfuryl Alcohol + Cyclic Solvent) at 298.2 K
• Phase Separation in Binary Mixtures Containing Linear Perfluoroalkanes
• Thermophysical Properties of Binary Mixtures of Cyclohexane + Nitrobenzene, Cyclohexanone + Nitrobenzene, and Cyclohexane + Cyclohexanone at (298.15, 303.15, and 308.15) K
• Vapor-Liquid Equilibria and Excess Enthalpies for Binary Systems of Dimethoxymethane with Hydrocarbons
• Measurement of Diffusion Coefficients in Thermodynamically Nonideal Systems
• Solubility of Propyl p-hydroxybenzoate in Supercritical Carbon Dioxide with and without Cosolvent
• Thermodynamic Properties of Binary Mixtures of p-Xylene with Cyclohexane, Heptane, Octane, and N-Methyl-2-pyrrolidone at Several Temperatures
• Determination of Activity Coefficients at Infinite Dilution of Polar and Nonpolar Solutes in the Ionic Liquid 1-Ethyl-3-methyl- imidazolium Bis(trifluoromethylsulfonyl) Imidate Using Gas-Liquid Chromatography at the Temperature 303.15 K or 318.15 K
• VLE and LLE Data for the System Cyclohexane + Cyclohexene + Water + Cyclohexanol
• 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
• Critical Properties of the Reacting Mixture in the Selective Oxidation of Cyclohexane by Oxygen in the Presence of Carbon Dioxide
• Dynamic Viscosities of the Binary Systems Cyclohexane and Cyclopentane with Acetone, Butanone, or 2-Pentanone at Three Temperatures T ) (293.15, 298.15, and 303.15) K
• Surface Properties of Dilute Solutions of Alkanes in Benzyl Alcohol
• Viscosities and Excess Molar Volumes of the Ternary System Toluene (1) + Cyclohexane (2) + Pentane (3) at 298.15 K
• Apparatus for the Determination of Water Solubility in Hydrocarbon: Toluene and Alkylcyclohexanes (C6 to C8) from 30 C to 180 C
• Liquid-Liquid Equilibria for Cyclohexane + Ethylbenzene + Sulfolane at (303.15, 313.15, and 323.15) K
• Solubility of p-Nitrobenzoic Acid in Supercritical Carbon Dioxide with and without Cosolvents
• 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
• Solubilities of Phenylphosphinic Acid, Hydroxymethylphenylphosphinic Acid, p-Methoxyphenylphosphinic Acid, p-Methoxyphenylhydroxymethylphosphinic Acid, Triphenylphosphine, Tri(p-methoxyphenyl)phosphine, and Tri(p-methoxyphenyl)phosphine Oxide in Selected Solvents
• Liquid-Liquid Equilibria for the Binary Systems of Sulfolane with Cycloalkanes
• 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
• Determination and Study of the Solubility of Methane in Mixtures of Methanol plus Various Hydrocarbons at High Pressures
• Liquid-Liquid Coexistence Curves for Binary Systems: Methanol + Cyclohexane and + Several Isomers of Hexane
• Viscosities, Densities, and Speed of Sound of the Cycloalkanes with Secondary Alcohols at T = (293.15, 298.15, and 303.15) K: New UNIFAC-VISCO Interaction Parameters
• Activity Coefficients at Infinite Dilution in 1-Alkyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
• Azeotropic and Heats of Mixing Data for Several Binary Organic Systems Containing 1-Methoxy-2-propanol and 2-Butoxy Ethanol
• Thermodynamic Properties of Mixtures Containing Ionic Liquids: Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Propyl Boronic Acid-3-Alkylimidazolium Bromide and 1-Propenyl-3-alkylimidazolium Bromide Using Inverse Gas Chromatography
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Liquid-Liquid Equilibria of Ternary and Six-Component Systems Including Cyclohexane, Benzene, Toluene, Ethylbenzene, Cumene, and Sulfolane at 303.15 K
• Isothermal Vapor-Liquid Equilibria and Excess Enthalpies of (Propyl Ethanoate + Heptane), (Propyl Ethanoate + Cyclohexane), and (Propyl Ethanoate + 1-Hexene)
• Solid-Liquid Equilibria for Binary Organic Systems Containing 1-Methoxy-2-propanol and 2-Butoxy Ethanol
• Infinite Dilution Activity Coefficients for Trihexyltetradecyl Phosphonium Ionic Liquids: Measurements and COSMO-RS Prediction
• Solubility of a-Carotene in Binary Solvents Formed by Some Hydrocarbons with 2,5,8-Trioxanonane, 2-Propanone, and Cyclohexanone
• Solubility of Anthracene in Binary Diisopropyl Ether + Alkane Solvent Mixtures at 298.15 K
• Viscosities and Interfacial Properties of I-Methyl-3-butylimidazolium Hexafluorophosphate and 1-Isobutenyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
• High-Pressure Density Measurements for the Binary System Cyclohexane + n-Hexadecane in the Temperature Range of (318.15 to 413.15) K
• Vapor-Liquid Equilibrium for Binary Systems of Cyclohexane + Cyclohexanone and + Cyclohexanol at Temperatures from (414.0 to 433.7) K
• Solubility of 5-(Dithiolan-3-yl)pentanoic Acid in the Mixed Solvents of Cyclohexane + Ethyl Acetate, Heptane + Ethyl Acetate, and Hexane + Ethyl Acetate
• Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Butyl-3-methyl-pyridinium Trifluoromethanesulfonate
• Cosolvent Selection for Benzene-Cyclohexane Separation in Extractive Distillation
• Solubilities of Phosphorus-Containing Compounds in Selected Solvents
• Densities, Excess Molar Volumes, Isothermal Compressibilities, and Isobaric Expansivities of Dimethyl Carbonate + Cyclohexane Systems at Temperatures from (293.15 to 313.15) K and Pressures from (0.1 to 40) MPa
• Determination of Activity Coefficients at Infinite Dilution of 35 Solutes in the Ionic Liquid, 1-Butyl-3-methylimidazolium Tosylate, Using Gas-Liquid Chromatography
• Vapor-Liquid Equilibrium Measurements and Modeling for Cyclohexane + Cyclohexanone
• Liquid Extraction of Benzene from Its Mixtures Using 1-Ethyl-3-methylimidazolium Ethylsulfate as a Solvent
• Activity Coefficients at Infinite Dilution for Hydrocarbons in Fatty Alcohols Determined by Gas-Liquid Chromatography
• Excess Gibbs Energies of the Ternary System 2-Methoxyethanol + Tetrahydrofuran + Cyclohexane and Other Relevant Binaries at 298.15 K
• Densities, Speeds of Sound, Excess Molar Volumes, and Excess Isentropic Compressibilities at T = (298.15 and 308.15) K for Methyl Methacrylate + 1-Alkanols (1-Butanol, 1-Pentanol, and 1-Heptanol) + Cyclohexane, + Benzene, + Toluene, + p-Xylene, and + Ethylbenzene
• Solubility of Benzoic Acid in Pure Solvents and Binary Mixtures
• Liquid-Liquid Equilibrium of (Water + Pentane-2,4-dione + Ethyl Ethanoate) and (Water + Pentane-2,4-dione + Cyclohexane) at (298.15 and 313.15) K
• Isobaric Vapor-Liquid Equilibria for Binary and Ternary Mixtures with Cyclohexane, Cyclohexene, and Methyl Isobutyl Ketone at 100 kPa
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Decyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Activity Coefficients at Infinite Dilution in Methylimidazolium Nitrate Ionic Liquids
• Measurements of Activity Coefficients at Infinite Dilution for Organic Solutes and Water in the Ionic Liquid 1-Butyl-1-methylpiperydinium Thiocyanate
• Influence of Anion Structure on the Liquid-Liquid Equilibria of 1-Ethyl-3-methyl-imidazolium Cation Based Ionic Liquid-Hydrocarbon Binary Systems
• Isothermal Vapor-Liquid Equilibrium for Methanol and 2,3-Dimethyl-1-butene at 343.06 K, 353.27 K, 363.19 K, and 372.90 K
• Measurement and Correlation for Solubilities of 16-Dehydropregnenolone Acetate in Different Solvents
• Gas Solubility in Binary Liquid Mixtures: Carbon Dioxide in Cyclohexane + Cyclohexanone
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Butyl-3-methylimidazolium Nitrate Using Gas-Liquid Chromatography
• Solubilities of 1-Hexyl-3-methylimidazole Nitrate and 1-Octyl-3-methylimidazole Nitrate in Selected Solvents
• Activity Coefficients at Infinite Dilution of Organic Compounds in Four New Imidazolium-Based Ionic Liquids
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Ethyl-3-methylimidazolium Diethylphosphate Using Gas Liquid Chromatography
• Apparent and Partial Molar Volumes at Infinite Dilution and Solid Liquid Equilibria of Dibenzothiophene + Alkane Systems
• Interfacial Tensions of Imidazolium-Based Ionic Liquids with N-Alkanes and Cyclohexane
• Partition Coefficients of Organic Compounds in Four New Tetraalkylammonium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Using Inverse Gas Chromatography
• Isobaric Vapor Liquid Equilibrium for Binary Systems of Toluene + Acrylic Acid, Toluene + Acetic Acid, and Cyclohexane + Acrylic Acid at 20 kPa
• Phase Equilibria Involved in the Extractive Distillation of Cyclohexane + Cyclohexene Using Diethyl Carbonate as an Entrainer
• Interactions of Volatile Organic Compounds with the Ionic Liquid 1-Butyl-1-methylpyrrolidinium Dicyanamide
• Vapor-Liquid Equilibria of Binary Mixtures Containing 1-Butanol and Hydrocarbons at 313.15 K
• Computer Aided Solvent scanning for the Separation of 2-methoxynaphthene and 2-acetyl-6-methoxynaphthalene
• Evaluation of the Performance of Trigeminal Tricationic Ionic Liquids for Separation Problems
• Vapor Liquid Equilibria of Binary Mixtures Containing 2-Butanol and Hydrocarbons at 313.15 K
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Dibutylphosphate Using Gas Liquid Chromatography
• Solubilities of Bis(2,4,6-trimethylbenzoyl)phenylphosphine Oxide in Different Organic Solvents at Several Temperatures
• Determination and Prediction of Vapor Liquid Equilibria for a System Containing Water + Butyl Acetate + Cyclohexane + Ethanol
• 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
• Liquid Liquid Extraction of Aromatic Compounds from Cycloalkanes Using 1-Butyl-3-methylimidazolium Methylsulfate Ionic Liquid
• Liquid Liquid Equilibria for Dipropylene Glycol Hydrocarbon Binary Systems: Experimental Data and Regression
• Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
• Solubilities of Adipic Acid in Acetic Acid + Water Mixtures and Acetic Acid + Cyclohexane Mixtures
• A Promising Ionic Liquid [BMIM][FeCl4] for the Extractive Separation of Aromatic and Aliphatic Hydrocarbons
• Solubilities of Rutaecarpine in Twelve Organic Solvents from (283.2 to 323.2) K
• Thermodynamics of Mixtures Containing Amines. XII. Volumetric and Speed of Sound Data at (293.15, 298.15, and 303.15) K for N-Methylaniline + Hydrocarbon Systems
• 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
• Vapor Liquid Equilibrium for Ternary and Binary Mixtures of Tetrahydrofuran, Cyclohexane, and 1,2-Propanediol at 101.3 kPa
• Liquid Liquid, Vapor Liquid, and Vapor Liquid Liquid Equilibrium Data for the Water n-Butanol Cyclohexane System at Atmospheric Pressure: Experimental Determination and Correlation
• Excess Molar Volume along with Viscosity and Refractive Index for Binary Systems of Tricyclo[5.2.1.0(2.6)]decane with Five Cycloalkanes
• Liquid Liquid Equilibrium for Ternary System Water + Cyclohexane + Acetic Acid at (303.2 to 333.2) K
• Solubility and Dissolution Thermodynamic Data of Mefenamic Acid Crystals in Different Classes of Organic Solvents
• Solubility of Dichloronitrobenzene in Eight Organic Solvents from T = (278.15 to 303.15) K: Measurement and Thermodynamic Modeling
• Excess Heat Capacities of Binary and Ternary Mixtures Containing 1-Ethyl-3-methylimidazolium Tetrafluoroborate and Anilines
• Infinite Dilution Activity Coefficients of Solutes Dissolved in Two Trihexyl(tetradecyl)phosphonium Ionic Liquids
• Experimental Measurements and Correlations of Excess Molar Enthalpies for the Binary and Ternary Mixtures of (Cyclohexane, 1,4-Dioxane and Piperidine) or (Cyclohexane, Morpholine and Piperidine) at 308.15 K and Atmospheric Pressure
• Solubilities of Succinic Acid in Acetic Acid + Water Mixtures and Acetic Acid + Cyclohexane Mixtures
• Design of a Gamma Densitometer for Hydrocarbon Fuel at High Temperature and Supercritical Pressure
• Solubility of Clopidogrel Hydrogen Sulfate (Form II) in Ethanol + Cyclohexane Mixtures at (283.35 to 333.75) K
• Liquid Liquid Equilibria at Three Temperatures (between 280.15 K and 333.15 K) of Binary, Ternary, and Quaternary Systems Involving Monoethylene Glycol, Water, Cyclohexane, para-Xylene, trans- and cis-Dimethylcyclohexane, and trans- and cis-Decahydronaphthalene
• Selective Separation of Aromatics from Paraffins and Cycloalkanes Using Morpholinium-Based Ionic Liquid
• Vapor Liquid Equilibrium Measurements and Thermodynamic Modeling of the System (Methane + Cyclohexane + Ethanol)
• Binary Liquid Liquid Equilibria of ?-Valerolactone with Some Hydrocarbons
• Deduction of Physicochemical Properties from Solubilities: 2,4-Dihydroxybenzophenone, Biotin, and Caprolactam as Examples
• Measurement and Correlation of Diffusion Coefficients of Aromatic Compounds at Infinite Dilution in Alkane and Cycloalkane Solvents
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Propyl-2,3-dimethylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Solubilities of Betulin in Fourteen Organic Solvents at Different Temperatures
• Liquid-Liquid Equilibria for Systems Composed by 1-Methyl-3-octylimidazolium Tetrafluoroborate Ionic Liquid, Thiophene, and n-Hexane or Cyclohexane
• Solid-Liquid Equilibria of Dibenzothiophene and Dibenzothiophene Sulfone in Organic Solvents
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas-Liquid Chromatography
• Isobaric Vapor-Liquid Equilibrium for the Binary Systems 1-Pentanol + Cyclohexane and 1-Pentanol + n-Hexane at Low Alcohol Compositions
• Solubilities of the Gaseous and Liquid Solutes and Their Thermodynamics of Solubilization in the Novel Room-Temperature Ionic Liquids at Infinite Dilution by Gas Chromatography
• Diffusion Coefficients of Organic Compounds at Infinite Dilution in Mixtures Involving Associating Compounds. Experimental Determination and Modeling by Group Contribution Methods
• Thermodynamics of Fuels with a Biosynthetic Component. II. Vapor Liquid Equilibrium Data for Binary and Ternary Mixtures Containing Ethyl 1,1-Dimethylethyl Ether, 1-Hexene, and Cyclohexane at T = 313.15 K
• Solubility of Losartan Potassium in Different Pure Solvents from (293.15 to 343.15) K
• Solubility of Losartan Potassium in Different Binary Solvents from (293.15 to 343.15) K
• Liquid-Liquid Equilibrium of Ternary Systems of Cyclohexane + (Benzene, + Toluene, + Ethylbenzene, or + o-Xylene) + 4-Methyl-N-butyl Pyridinium Tetrafluoroborate Ionic Liquid at 303.15 K
• Liquid-Liquid Equilibrium for 2,2,2-Trifluoroethanol + Ethanol + Cyclohexane from (288.15 to 308.15) K
• Phase Equilibrium Properties of Binary and Ternary Mixtures Containing Dibutyl Ether, Cyclohexane, and Heptane or 1-Hexene at T ) 313.15 K
• Liquid-Liquid Equilibria for Benzene + Cyclohexane + 1-Methyl-3-methylimidazolium Dimethylphosphate or + 1-Ethyl-3-methylimidazolium Diethylphosphate
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Hexyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas-Liquid Chromatography
• Enthalpies of Vaporization and Vapor Pressures of Some Deuterated Hydrocarbons. Liquid-Vapor Pressure Isotope Effects
• 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
• Phase Behavior of the Reactant and Products of Cyclohexane Oxidation in Compressed CO2
• Liquid-Liquid Equilibrium of (Cyclohexane + 2,2,2-Trifluoroethanol) and (Cyclohexane + Methanol) from (278.15 to 318.15) K
• Determination and Correlation of Excess Molar Enthalpies of Eight Binary Systems Containing Acetophenone at Different Temperatures
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Ethyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Solubility of Diamantane, Trimantane, Tetramantane, and Their Derivatives in Organic Solvents
• Effect of Temperature on Phase Equilibrium of the Mixed-Solvent System of (2,2,2-Trifluoroethanol + Methanol + Cyclohexane)
• Densities and Viscosities of Binary Mixtures of Tri-n-butyl Phosphate + Cyclohexane, + n-Heptane at T ) (288.15, 293.15, 298.15, 303.15, and 308.15) K
• Ternary Liquid-Liquid Equilibria Measurement for Benzene + Cyclohexane + N-Methylimidazole, or N-Ethylimidazole, or N-Methylimidazolium Dibutylphosphate at 298.2 K and Atmospheric Pressure
• Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
• Solubility of Artemisinin in Seven Different Pure Solvents from (283.15 to 323.15) K
• Densities and Viscosities of Binary Mixtures of Tris(2-ethylhexyl) Phosphate + Cyclohexane or n-Hexane at T ) (293.15, 298.15, and 303.15) K and p ) 0.1 MPa
• Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Inverse Gas Chromatography
• Densities and Viscosities of Ternary Mixtures of Cyclohexane + Cyclohexanone + Some Alkyl Acetates at 298.15 K
• Excess Enthalpies of Binary and Ternary Mixtures Containing Dibutyl Ether, Cyclohexane, and 1-Butanol at 298.15 K
• Activity Coefficients at Infinite Dilution of Organic Compounds in Trihexyl(tetradecyl)phosphonium Bis(trifluoromethylsulfonyl)imide Using Inverse Gas Chromatography
• Solubility of Canthaxanthin in Pure Solvents from (293.15 to 343.15) K
• Liquid Viscosities of Cyclohexane, Cyclohexane + Tetradecane, and Cyclohexane + Benzene from (313 to 393) K and Pressures Up to 60 MPa
• Volumetric Behavior of the Binary Mixtures of Methyl Ethyl Ketone with n-Hexane, Cyclohexane, and Benzene at T ) (303.15, 313.15, and 323.15) K
• Liquid Viscosities of the Ternary System Benzene + Cyclohexane + n-Tetradecane from (313 to 393) K and Pressures up to 60 MPa
• Density, Speed of Sound, and Refractive Index for Binary Mixtures Containing Cycloalkanes and Aromatic Compounds at T = 313.15 K
• Density and Viscosity of Decalin, Cyclohexane, and Toluene Binary Mixtures at (283.15, 293.15, 303.15, 313.15, and 323.15) K
• High-Pressure Viscosity Measurements for the Binary System Cyclohexane + n-Hexadecane in the Temperature Range of (318.15 to 413.15) K
• Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
• Excess Molar Enthalpies for the Binary and Ternary Mixtures of Cyclohexane, Tetrahydropyran, and 1,4-Dioxane at 308.15 K and Atmospheric Pressure: Experimental Measurements and Correlations
• Isobaric Vapor-Liquid Equilibria for Binary and Ternary Mixtures with Cyclohexane, Cyclohexene, and 2-Methoxyethanol at 100 kPa
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-(2-Hydroxyethyl)-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
• Liquid-Liquid Equilibria for Benzene + Cyclohexane + 1-Butyl-3-methylimidazolium Hexafluorophosphate
• Excess Molar Enthalpies for the Binary and Ternary Mixtures of Cyclohexane, Tetrahydropyran, and Piperidine at 308.15 K and Atmospheric Pressure: Experimental Measurements and Correlations
• Comparison of the Efficiencies of Amine Extractants on Lactic Acid with Different Organic Solvents
• Phase Equilibria of (1-Hexyl-3-methylimidazolium Thiocyanate + Water, Alcohol, or Hydrocarbon) Binary Systems
• Density, Speed of Sound, and Refractive Index of the Binary Systems Cyclohexane (1) or Methylcyclohexane (1) or Cyclo-octane (1) with Benzene (2), Toluene (2), and Ethylbenzene (2) at Two Temperatures
• (Liquid + Liquid) Equilibria of (Cyclohexane + Dimethyl Sulfoxide + Cyclohexanone) and (Cyclohexane + Dimethyl Sulfoxide + Cyclohexanol) at T = 303.2 K
• Phase Equilibria for Liquid Mixtures of (an Alkane + Toluene + Dimethyl Phthalate)
• Isobaric Vapor-Liquid-Liquid Equilibrium and Vapor-Liquid Equilibrium for the Quaternary System Water-Ethanol-Cyclohexane-Isooctane at 101.3 kPa
• Density, Viscosity, and Speed of Sound of (Methyl Benzoate + Cyclohexane), (Methyl Benzoate + n-Hexane), (Methyl Benzoate + Heptane), and (Methyl Benzoate + Octane) at Temperatures of (303.15, 308.15, and 313.15) K
• Isobaric Vapor-Liquid Equilibria for (Acetic Acid + Cyclohexane) and (Cyclohexane + Acetylacetone) at a Pressure of 101.3 kPa and for (Acetic Acid + Acetylacetone) at a Pressure of 60.0 kPa
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in Glycerol Using Gas-Liquid Chromatography
• Study of Ether-, Alcohol-, or Cyano-Functionalized Ionic Liquids Using Inverse Gas Chromatography
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Ethyl-3-methylimidazolium Tris(pentafluoroethyl)trifluorophosphate [EMIM][FAP] Using Gas-Liquid Chromatography
• Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Hexyl-3-methylimidazolium Thiocyanate
• Experimental Measurements and Correlations of Excess Molar Enthalpies for the Binary and Ternary Mixtures of (Cyclohexane, Tetrahydropyran, and Morpholine) or (Cyclohexane, 1,4-Dioxane, and Morpholine) at 308.15 K and Atmospheric Pressure
• Density, Speed of Sound, and Refractive Index for Binary Mixtures Containing Cycloalkanes with o-Xylene, m-Xylene, p-Xylene, and Mesitylene at T = (298.15 and 313.15) K
• Solubility of Triadimefon in Organic Solvents at Temperatures between (288.15 and 333.15) K
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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