Chemical Properties of 1-Propanol (CAS 71-23-8)

InChI

InChI=1S/C3H8O/c1-2-3-4/h4H,2-3H2,1H3

InChI Key

BDERNNFJNOPAEC-UHFFFAOYSA-N

Formula

C3H8O

SMILES

CCCO

Molecular Weight¹

60.09

CAS

71-23-8

Other Names

• 1-Hydroxypropane
• 1-Propyl alcohol
• Alcohol, propyl
• Alcool propilico
• Alcool propylique
• Ethylcarbinol
• N-PROPYL ALCOHOL
• NSC 30300
• Optal
• Osmosol extra
• PROPYL ALCOHOL
• Propan-1-ol
• Propanol
• Propanol-1
• Propanole
• Propanolen
• Propanoli
• Propylan-propyl alcohol
• Propylic alcohol
• Propylowy alkohol
• UN 1274
• n-C3H7OH
• n-Propan-1-ol
• n-Propanol
• n-Propyl alkohol

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• T_ig : Autoignition Temperature (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).
• C_p,solid : Solid 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,cc : Flash Point (Closed Cup Method) (K).
• T_flash,oc : Flash Point (Open Cup Method) (K).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• R_g : Radius of Gyration.
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_gas : Molar entropy at standard conditions (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• c_sound,fluid : Speed of sound in fluid (m/s).
• γ : Surface Tension (N/m).
• S°_{solid,1 bar} : Solid phase molar entropy at standard conditions (J/mol×K).
• T_boil : Normal Boiling Point Temperature (K).
• T_boil : Boiling point at given pressure (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• V_c : Critical Volume (m³/kmol).
• 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	0.6230		KDB
PAff	786.50	kJ/mol	NIST
Tig	644.26	K	KDB
BasG	756.10	kJ/mol	NIST
ΔcH°liquid	[-2032.59; -2017.70]	kJ/mol
ΔcH°liquid	-2021.31 ± 0.25	kJ/mol	NIST
ΔcH°liquid	-2019.40 ± 0.30	kJ/mol	NIST
ΔcH°liquid	-2021.40 ± 0.75	kJ/mol	NIST
ΔcH°liquid	-2017.70 ± 1.00	kJ/mol	NIST
ΔcH°liquid	-2032.59	kJ/mol	NIST
Cp,liquid	143.41	J/mol×K	THERMOD...
μ	1.70	debye	KDB
η	0.0019544	Pa×s	Densiti...
LFL	2.10	% in Air	KDB
UFL	13.50	% in Air	KDB
Tflash,cc	300.37	K	KDB
Tflash,oc	298.15	K	KDB
ΔfG°	-161.90	kJ/mol	KDB
Rg	2.7360		KDB
ΔfH°gas	[-258.80; -254.70]	kJ/mol
ΔfH°gas	-256.60	kJ/mol	KDB
ΔfH°gas	-255.10	kJ/mol	NIST
ΔfH°gas	-255.20 ± 0.30	kJ/mol	NIST
ΔfH°gas	-255.60 ± 1.30	kJ/mol	NIST
ΔfH°gas	-257.20	kJ/mol	NIST
ΔfH°gas	-257.30 ± 0.40	kJ/mol	NIST
ΔfH°gas	-254.70 ± 4.40	kJ/mol	NIST
ΔfH°gas	-258.80 ± 1.10	kJ/mol	NIST
ΔfH°liquid	[-306.30; -302.50]	kJ/mol
ΔfH°liquid	-302.54 ± 0.25	kJ/mol	NIST
ΔfH°liquid	-303.00 ± 1.30	kJ/mol	NIST
ΔfH°liquid	-304.60 ± 0.40	kJ/mol	NIST
ΔfH°liquid	-302.50 ± 4.20	kJ/mol	NIST
ΔfH°liquid	-306.30 ± 1.00	kJ/mol	NIST
ΔfusH°	5.40	kJ/mol	Heat Ca...
ΔvapH°	38.95	kJ/mol	Joback Calculated Property
IE	[10.00; 10.52]	eV
IE	10.22 ± 0.06	eV	NIST
IE	10.22 ± 0.07	eV	NIST
IE	10.00	eV	NIST
IE	10.15 ± 0.03	eV	NIST
IE	10.16 ± 0.03	eV	NIST
IE	10.32 ± 0.02	eV	NIST
IE	10.25	eV	NIST
IE	10.22 ± 0.04	eV	NIST
IE	10.20	eV	NIST
IE	10.51	eV	NIST
IE	10.52 ± 0.03	eV	NIST
IE	10.51	eV	NIST
IE	10.49	eV	NIST
IE	10.48	eV	NIST
log10WS	[0.62; 0.62]
log10WS	0.62		Aq. Sol...
log10WS	0.62		Estimat...
logPoct/wat	0.389		Crippen Calculated Property
McVol	59.000	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
NFPA Health	1		KDB
Pc	[5082.00; 5397.00]	kPa
Pc	5169.00	kPa	KDB
Pc	5170.00 ± 20.00	kPa	NIST
Pc	5170.00	kPa	NIST
Pc	5168.00 ± 20.00	kPa	NIST
Pc	5168.00 ± 20.00	kPa	NIST
Pc	5170.00	kPa	NIST
Pc	5182.00 ± 10.00	kPa	NIST
Pc	5155.00	kPa	NIST
Pc	5170.00	kPa	NIST
Pc	5082.00	kPa	NIST
Pc	5218.00	kPa	NIST
Pc	5082.00	kPa	NIST
Pc	Outlier 5397.00	kPa	NIST
Inp	[507.00; 595.00]
Inp	561.20		NIST
Inp	561.40		NIST
Inp	559.30		NIST
Inp	558.20		NIST
Inp	549.70		NIST
Inp	543.70		NIST
Inp	536.90		NIST
Inp	Outlier 521.00		NIST
Inp	544.60		NIST
Inp	542.30		NIST
Inp	540.50		NIST
Inp	541.50		NIST
Inp	556.50		NIST
Inp	553.60		NIST
Inp	551.40		NIST
Inp	544.60		NIST
Inp	542.30		NIST
Inp	540.50		NIST
Inp	541.50		NIST
Inp	556.50		NIST
Inp	553.50		NIST
Inp	551.40		NIST
Inp	565.00		NIST
Inp	575.00		NIST
Inp	546.00		NIST
Inp	555.00		NIST
Inp	530.00		NIST
Inp	539.90		NIST
Inp	530.00		NIST
Inp	544.00		NIST
Inp	525.00		NIST
Inp	562.00		NIST
Inp	Outlier 520.00		NIST
Inp	547.00		NIST
Inp	523.00		NIST
Inp	574.00		NIST
Inp	561.00		NIST
Inp	555.00		NIST
Inp	Outlier 595.00		NIST
Inp	551.00		NIST
Inp	568.00		NIST
Inp	560.00		NIST
Inp	568.00		NIST
Inp	568.00		NIST
Inp	524.00		NIST
Inp	Outlier 521.00		NIST
Inp	551.00		NIST
Inp	555.00		NIST
Inp	557.00		NIST
Inp	556.00		NIST
Inp	537.00		NIST
Inp	540.20		NIST
Inp	540.20		NIST
Inp	546.00		NIST
Inp	552.00		NIST
Inp	532.00		NIST
Inp	552.00		NIST
Inp	552.00		NIST
Inp	536.00		NIST
Inp	533.00		NIST
Inp	530.00		NIST
Inp	537.00		NIST
Inp	544.00		NIST
Inp	535.00		NIST
Inp	Outlier 507.00		NIST
Inp	557.00		NIST
Inp	561.00		NIST
Inp	549.00		NIST
Inp	553.00		NIST
Inp	536.00		NIST
Inp	559.00		NIST
Inp	559.00		NIST
Inp	559.00		NIST
Inp	548.00		NIST
Inp	557.90		NIST
Inp	568.00		NIST
Inp	568.00		NIST
Inp	568.00		NIST
Inp	554.00		NIST
Inp	553.00		NIST
Inp	560.00		NIST
Inp	539.00		NIST
Inp	538.64		NIST
Inp	Outlier 521.00		NIST
Inp	535.00		NIST
Inp	548.00		NIST
Inp	561.00		NIST
Inp	555.00		NIST
Inp	568.00		NIST
Inp	547.00		NIST
Inp	544.00		NIST
Inp	548.00		NIST
Inp	544.00		NIST
Inp	557.00		NIST
Inp	558.00		NIST
Inp	551.00		NIST
Inp	544.00		NIST
Inp	548.00		NIST
Inp	548.00		NIST
Inp	535.00		NIST
Inp	570.00		NIST
Inp	560.00		NIST
Inp	539.00		NIST
Inp	560.00		NIST
Inp	562.00		NIST
Inp	543.00		NIST
Inp	546.00		NIST
Inp	546.00		NIST
Inp	539.00		NIST
Inp	571.00		NIST
Inp	534.00		NIST
Inp	555.00		NIST
Inp	535.00		NIST
Inp	Outlier 581.00		NIST
Inp	571.00		NIST
Inp	572.00		NIST
Inp	561.20		NIST
Inp	543.70		NIST
Inp	540.50		NIST
Inp	544.60		NIST
Inp	553.50		NIST
Inp	555.00		NIST
Inp	525.00		NIST
Inp	561.00		NIST
Inp	557.00		NIST
Inp	559.00		NIST
Inp	568.00		NIST
Inp	560.00		NIST
Inp	548.00		NIST
I	[988.00; 1086.00]
I	1046.00		NIST
I	1037.00		NIST
I	1031.00		NIST
I	1024.00		NIST
I	1037.60		NIST
I	1046.90		NIST
I	1051.70		NIST
I	1054.90		NIST
I	Outlier 1072.00		NIST
I	Outlier 988.00		NIST
I	1000.00		NIST
I	Outlier 997.00		NIST
I	1040.00		NIST
I	1035.00		NIST
I	Outlier 993.00		NIST
I	1031.00		NIST
I	1030.00		NIST
I	1046.00		NIST
I	1036.00		NIST
I	1026.00		NIST
I	1056.00		NIST
I	1021.00		NIST
I	1014.00		NIST
I	Outlier 993.00		NIST
I	1037.00		NIST
I	1030.00		NIST
I	1043.00		NIST
I	1005.00		NIST
I	1002.00		NIST
I	1025.00		NIST
I	1037.00		NIST
I	1060.00		NIST
I	1061.00		NIST
I	1030.00		NIST
I	1049.00		NIST
I	1049.00		NIST
I	1025.00		NIST
I	1015.00		NIST
I	1038.00		NIST
I	1026.00		NIST
I	1045.00		NIST
I	1041.00		NIST
I	1052.00		NIST
I	1040.00		NIST
I	1045.00		NIST
I	Outlier 1073.00		NIST
I	1041.00		NIST
I	1038.00		NIST
I	1038.00		NIST
I	1064.00		NIST
I	1049.00		NIST
I	1025.00		NIST
I	1025.00		NIST
I	1031.00		NIST
I	1052.00		NIST
I	1052.00		NIST
I	1051.00		NIST
I	1052.00		NIST
I	1052.00		NIST
I	1037.00		NIST
I	1029.00		NIST
I	1041.00		NIST
I	1032.00		NIST
I	1034.00		NIST
I	1031.00		NIST
I	1033.00		NIST
I	1028.00		NIST
I	1023.00		NIST
I	1040.00		NIST
I	1037.00		NIST
I	1045.00		NIST
I	1034.00		NIST
I	1025.00		NIST
I	1035.00		NIST
I	1002.00		NIST
I	1030.00		NIST
I	1030.00		NIST
I	1043.00		NIST
I	1037.00		NIST
I	1029.00		NIST
I	1025.00		NIST
I	1040.00		NIST
I	1038.00		NIST
I	1045.00		NIST
I	1006.00		NIST
I	1038.00		NIST
I	1032.00		NIST
I	1002.00		NIST
I	1069.00		NIST
I	1046.00		NIST
I	1049.00		NIST
I	1002.00		NIST
I	1042.00		NIST
I	1022.00		NIST
I	1002.00		NIST
I	1030.00		NIST
I	Outlier 990.00		NIST
I	Outlier 996.00		NIST
I	Outlier 990.00		NIST
I	Outlier 996.00		NIST
I	1042.00		NIST
I	1040.00		NIST
I	1036.00		NIST
I	1038.00		NIST
I	1045.00		NIST
I	Outlier 992.00		NIST
I	1030.00		NIST
I	1036.00		NIST
I	Outlier 1086.00		NIST
I	1036.00		NIST
I	1036.00		NIST
I	1051.00		NIST
I	1052.00		NIST
I	1046.00		NIST
I	1036.00		NIST
I	1036.00		NIST
I	1036.00		NIST
I	1032.00		NIST
I	1035.00		NIST
I	1044.00		NIST
I	1036.00		NIST
I	1038.00		NIST
I	1042.00		NIST
I	1036.00		NIST
I	1042.00		NIST
I	1042.00		NIST
I	1047.00		NIST
I	1042.00		NIST
I	1025.00		NIST
I	1027.00		NIST
I	1031.00		NIST
I	1002.00		NIST
I	Outlier 1072.00		NIST
I	1033.00		NIST
I	1033.00		NIST
I	1014.00		NIST
I	1040.00		NIST
I	1030.00		NIST
I	1051.00		NIST
I	1036.00		NIST
I	1038.00		NIST
I	1047.00		NIST
I	1002.00		NIST
I	1037.00		NIST
I	1025.00		NIST
I	1049.00		NIST
I	1026.00		NIST
I	1045.00		NIST
I	1064.00		NIST
I	1052.00		NIST
I	1031.00		NIST
I	1046.00		NIST
I	1046.90		NIST
I	1000.00		NIST
I	1056.00		NIST
S°gas	322.49	J/mol×K	NIST
S°liquid	[192.80; 214.20]	J/mol×K
S°liquid	192.80	J/mol×K	NIST
S°liquid	214.20	J/mol×K	NIST
S°solid,1 bar	112.70	J/mol×K	NIST
Tboil	[355.30; 371.25]	K
Tboil	370.30	K	KDB
Tboil	370.40	K	Excess ...
Tboil	370.44	K	Isobari...
Tboil	370.31	K	Isobari...
Tboil	370.35	K	Isobari...
Tboil	370.20	K	Heterog...
Tboil	369.75	K	Isobari...
Tboil	370.45	K	(Vapour...
Tboil	370.35	K	Isobari...
Tboil	369.90	K	Separat...
Tboil	370.35	K	Measure...
Tboil	370.33	K	Isobari...
Tboil	370.30	K	Isobari...
Tboil	370.31	K	Measure...
Tboil	370.19	K	Vapor-L...
Tboil	370.21	K	Vapor-L...
Tboil	370.24	K	Vapor-L...
Tboil	370.05	K	P, rho,...
Tboil	370.40	K	Evaluat...
Tboil	370.21	K	Vapor-L...
Tboil	370.21	K	Vapor L...
Tboil	370.30 ± 0.20	K	NIST
Tboil	370.26 ± 0.20	K	NIST
Tboil	370.26 ± 0.20	K	NIST
Tboil	370.20 ± 0.40	K	NIST
Tboil	370.26 ± 0.20	K	NIST
Tboil	370.26 ± 0.20	K	NIST
Tboil	370.28 ± 0.08	K	NIST
Tboil	370.30 ± 0.20	K	NIST
Tboil	370.40 ± 0.20	K	NIST
Tboil	370.30 ± 0.30	K	NIST
Tboil	370.10 ± 0.25	K	NIST
Tboil	370.60	K	NIST
Tboil	370.50 ± 0.20	K	NIST
Tboil	370.30	K	NIST
Tboil	370.40 ± 0.40	K	NIST
Tboil	370.40 ± 0.30	K	NIST
Tboil	370.40 ± 0.30	K	NIST
Tboil	370.15 ± 0.50	K	NIST
Tboil	370.60 ± 0.30	K	NIST
Tboil	370.30 ± 0.50	K	NIST
Tboil	370.32 ± 0.06	K	NIST
Tboil	370.30 ± 0.50	K	NIST
Tboil	370.40 ± 0.30	K	NIST
Tboil	370.29 ± 0.30	K	NIST
Tboil	370.30 ± 0.50	K	NIST
Tboil	370.30 ± 0.50	K	NIST
Tboil	370.35 ± 0.20	K	NIST
Tboil	370.23 ± 0.12	K	NIST
Tboil	370.50 ± 0.30	K	NIST
Tboil	370.35 ± 0.30	K	NIST
Tboil	370.35	K	NIST
Tboil	370.35 ± 0.30	K	NIST
Tboil	370.25 ± 0.20	K	NIST
Tboil	370.44 ± 0.15	K	NIST
Tboil	370.30 ± 0.05	K	NIST
Tboil	370.40 ± 0.20	K	NIST
Tboil	370.23 ± 0.20	K	NIST
Tboil	370.00 ± 1.50	K	NIST
Tboil	370.00 ± 1.00	K	NIST
Tboil	370.35 ± 0.30	K	NIST
Tboil	370.38 ± 0.10	K	NIST
Tboil	370.60 ± 0.30	K	NIST
Tboil	370.34 ± 0.30	K	NIST
Tboil	370.40 ± 0.30	K	NIST
Tboil	370.70 ± 1.00	K	NIST
Tboil	366.70 ± 3.00	K	NIST
Tboil	370.60 ± 0.30	K	NIST
Tboil	370.00 ± 1.00	K	NIST
Tboil	370.40 ± 0.50	K	NIST
Tboil	370.00 ± 0.50	K	NIST
Tboil	370.59 ± 0.33	K	NIST
Tboil	370.40 ± 0.20	K	NIST
Tboil	370.20 ± 0.30	K	NIST
Tboil	370.30 ± 0.20	K	NIST
Tboil	368.70 ± 1.00	K	NIST
Tboil	370.40 ± 0.30	K	NIST
Tboil	368.60 ± 1.00	K	NIST
Tboil	370.00 ± 1.00	K	NIST
Tboil	370.40 ± 0.50	K	NIST
Tboil	370.60 ± 0.50	K	NIST
Tboil	370.34 ± 0.20	K	NIST
Tboil	367.60 ± 1.00	K	NIST
Tboil	370.00 ± 1.00	K	NIST
Tboil	369.60 ± 0.50	K	NIST
Tboil	Outlier 355.40 ± 0.30	K	NIST
Tboil	370.10 ± 0.50	K	NIST
Tboil	370.40 ± 0.50	K	NIST
Tboil	370.40 ± 0.40	K	NIST
Tboil	370.40 ± 0.30	K	NIST
Tboil	370.40 ± 0.30	K	NIST
Tboil	371.20 ± 0.50	K	NIST
Tboil	370.70 ± 0.60	K	NIST
Tboil	370.40 ± 0.50	K	NIST
Tboil	370.50 ± 0.50	K	NIST
Tboil	Outlier 355.30 ± 0.50	K	NIST
Tboil	369.60 ± 1.00	K	NIST
Tboil	369.80 ± 0.40	K	NIST
Tboil	371.00 ± 0.30	K	NIST
Tboil	370.30 ± 0.20	K	NIST
Tboil	369.60 ± 1.00	K	NIST
Tboil	370.35 ± 0.03	K	NIST
Tboil	370.95 ± 0.10	K	NIST
Tboil	370.30 ± 0.30	K	NIST
Tboil	370.30 ± 0.05	K	NIST
Tboil	370.40 ± 0.10	K	NIST
Tboil	370.34 ± 0.07	K	NIST
Tboil	370.40 ± 0.50	K	NIST
Tboil	370.60 ± 0.50	K	NIST
Tboil	370.50 ± 0.50	K	NIST
Tboil	370.40 ± 0.30	K	NIST
Tboil	370.50 ± 0.50	K	NIST
Tboil	370.70 ± 0.50	K	NIST
Tboil	370.40 ± 0.50	K	NIST
Tboil	370.40 ± 0.50	K	NIST
Tboil	370.40 ± 0.50	K	NIST
Tboil	370.70 ± 1.00	K	NIST
Tboil	370.31 ± 0.30	K	NIST
Tboil	370.40 ± 0.50	K	NIST
Tboil	370.70 ± 1.00	K	NIST
Tboil	370.40 ± 0.30	K	NIST
Tboil	371.00 ± 0.30	K	NIST
Tboil	370.50 ± 0.50	K	NIST
Tboil	370.20 ± 0.50	K	NIST
Tboil	370.34 ± 0.10	K	NIST
Tboil	370.60 ± 0.50	K	NIST
Tboil	370.90 ± 0.20	K	NIST
Tboil	370.13 ± 0.20	K	NIST
Tboil	370.30 ± 0.20	K	NIST
Tboil	371.25 ± 0.20	K	NIST
Tboil	370.34 ± 0.05	K	NIST
Tboil	370.33 ± 0.05	K	NIST
Tboil	370.35 ± 0.05	K	NIST
Tboil	370.40 ± 0.50	K	NIST
Tboil	370.20 ± 0.50	K	NIST
Tboil	369.80 ± 0.30	K	NIST
Tboil	369.90 ± 0.50	K	NIST
Tboil	370.40 ± 0.30	K	NIST
Tboil	370.37 ± 0.10	K	NIST
Tboil	369.60 ± 1.00	K	NIST
Tboil	370.30 ± 0.50	K	NIST
Tboil	370.60 ± 0.30	K	NIST
Tboil	370.41 ± 0.20	K	NIST
Tboil	370.40 ± 0.30	K	NIST
Tboil	370.40 ± 0.30	K	NIST
Tboil	370.50 ± 0.50	K	NIST
Tboil	370.00 ± 1.00	K	NIST
Tboil	368.70 ± 0.50	K	NIST
Tboil	370.34 ± 0.20	K	NIST
Tboil	369.80 ± 0.50	K	NIST
Tboil	370.40 ± 0.50	K	NIST
Tboil	370.40 ± 0.10	K	NIST
Tboil	369.20 ± 0.10	K	NIST
Tboil	369.30 ± 0.50	K	NIST
Tboil	369.90 ± 2.00	K	NIST
Tboil	369.75 ± 0.50	K	NIST
Tboil	371.00 ± 1.00	K	NIST
Tboil	371.00 ± 0.50	K	NIST
Tboil	370.60 ± 0.50	K	NIST
Tboil	370.56 ± 0.30	K	NIST
Tboil	Outlier 363.00 ± 4.00	K	NIST
Tc	[536.80; 537.00]	K
Tc	536.80	K	KDB
Tc	537.00	K	Measure...
Tc	537.00	K	Measure...
Tfus	[146.62; 147.00]	K
Tfus	147.00	K	KDB
Tfus	146.62	K	Aq. Sol...
Tfus	146.70	K	Phase e...
Tfus	146.95	K	NIST
Tfus	146.70 ± 0.50	K	NIST
Tfus	147.00 ± 3.00	K	NIST
Ttriple	[147.00; 148.75]	K
Ttriple	148.75	K	KDB
Ttriple	148.75 ± 0.02	K	NIST
Ttriple	148.75 ± 0.02	K	NIST
Ttriple	147.00 ± 0.30	K	NIST
Vc	[0.216; 0.218]	m3/kmol
Vc	0.218	m3/kmol	KDB
Vc	0.218	m3/kmol	NIST
Vc	0.216 ± 0.001	m3/kmol	NIST
Zc	0.2524720		KDB
Zra	0.25		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[102.26; 148.95]	J/mol×K	[371.20; 603.25]
Cp,gas	102.26 ± 0.20	J/mol×K	371.20	NIST
Cp,gas	107.28 ± 0.96	J/mol×K	375.45	NIST
Cp,gas	108.67 ± 0.96	J/mol×K	383.05	NIST
Cp,gas	109.42 ± 0.96	J/mol×K	387.15	NIST
Cp,gas	106.44 ± 0.21	J/mol×K	391.20	NIST
Cp,gas	111.21 ± 0.96	J/mol×K	396.95	NIST
Cp,gas	113.59 ± 0.96	J/mol×K	409.95	NIST
Cp,gas	110.42 ± 0.22	J/mol×K	411.20	NIST
Cp,gas	115.56 ± 0.96	J/mol×K	420.75	NIST
Cp,gas	115.97 ± 0.96	J/mol×K	422.95	NIST
Cp,gas	114.35 ± 0.23	J/mol×K	431.20	NIST
Cp,gas	118.71 ± 0.96	J/mol×K	437.95	NIST
Cp,gas	118.62 ± 0.24	J/mol×K	451.20	NIST
Cp,gas	122.94 ± 0.96	J/mol×K	461.05	NIST
Cp,gas	125.55 ± 0.96	J/mol×K	475.35	NIST
Cp,gas	130.97 ± 0.96	J/mol×K	504.95	NIST
Cp,gas	132.23 ± 0.96	J/mol×K	511.85	NIST
Cp,gas	135.98 ± 0.96	J/mol×K	532.35	NIST
Cp,gas	141.05 ± 0.96	J/mol×K	560.05	NIST
Cp,gas	144.49 ± 0.96	J/mol×K	578.85	NIST
Cp,gas	148.95 ± 0.96	J/mol×K	603.25	NIST
Cp,liquid	[131.30; 192.90]	J/mol×K	[270.00; 333.15]
Cp,liquid	136.00	J/mol×K	270.00	NIST
Cp,liquid	131.30	J/mol×K	274.60	NIST
Cp,liquid	133.50	J/mol×K	275.00	NIST
Cp,liquid	133.50	J/mol×K	275.40	NIST
Cp,liquid	139.00	J/mol×K	288.15	Excess ...
Cp,liquid	138.40	J/mol×K	288.15	NIST
Cp,liquid	142.30	J/mol×K	293.15	Excess ...
Cp,liquid	141.80	J/mol×K	293.15	NIST
Cp,liquid	144.60	J/mol×K	298.00	NIST
Cp,liquid	146.10	J/mol×K	298.00	NIST
Cp,liquid	144.80	J/mol×K	298.00	NIST
Cp,liquid	192.90	J/mol×K	298.10	NIST
Cp,liquid	145.60	J/mol×K	298.10	NIST
Cp,liquid	144.06	J/mol×K	298.15	NIST
Cp,liquid	144.44	J/mol×K	298.15	NIST
Cp,liquid	144.90	J/mol×K	298.15	Excess ...
Cp,liquid	146.88	J/mol×K	298.15	NIST
Cp,liquid	143.80	J/mol×K	298.15	NIST
Cp,liquid	143.96	J/mol×K	298.15	NIST
Cp,liquid	149.00	J/mol×K	298.15	NIST
Cp,liquid	143.78	J/mol×K	298.15	NIST
Cp,liquid	143.87	J/mol×K	298.15	NIST
Cp,liquid	143.77	J/mol×K	298.15	NIST
Cp,liquid	146.34	J/mol×K	298.22	NIST
Cp,liquid	164.80	J/mol×K	301.20	NIST
Cp,liquid	140.21	J/mol×K	303.00	NIST
Cp,liquid	148.20	J/mol×K	303.15	Excess ...
Cp,liquid	147.90	J/mol×K	303.40	NIST
Cp,liquid	151.00	J/mol×K	308.15	Excess ...
Cp,liquid	153.70	J/mol×K	313.15	Excess ...
Cp,liquid	158.60	J/mol×K	313.20	NIST
Cp,liquid	157.10	J/mol×K	318.15	Excess ...
Cp,liquid	155.60	J/mol×K	320.00	NIST
Cp,liquid	160.10	J/mol×K	323.15	Excess ...
Cp,liquid	164.50	J/mol×K	328.15	Excess ...
Cp,liquid	167.80	J/mol×K	333.15	Excess ...
Cp,solid	106.30	J/mol×K	150.00	NIST
η	[0.0005150; 0.0034744]	Pa×s	[283.15; 363.15]
η	0.0034744	Pa×s	283.15	Density...
η	0.0027676	Pa×s	288.15	Density...
η	0.0024202	Pa×s	288.15	Densiti...
η	0.0025070	Pa×s	288.15	Densiti...
η	0.0021900	Pa×s	293.00	Ultraso...
η	0.0022720	Pa×s	293.15	Densiti...
η	0.0021590	Pa×s	293.15	Viscosi...
η	0.0022050	Pa×s	293.15	Viscosi...
η	0.0021412	Pa×s	293.15	Densiti...
η	0.0022380	Pa×s	293.15	Density...
η	0.0021920	Pa×s	293.15	Densiti...
η	0.0021590	Pa×s	293.15	Dynamic...
η	0.0024104	Pa×s	293.15	Density...
η	0.0021940	Pa×s	293.15	Viscosi...
η	0.0021880	Pa×s	293.15	Density...
η	0.0021372	Pa×s	293.15	Densiti...
η	0.0022060	Pa×s	293.15	Propert...
η	0.0022020	Pa×s	293.15	Densiti...
η	0.0022040	Pa×s	293.15	Thermod...
η	0.0019400	Pa×s	298.15	Tempera...
η	0.0019550	Pa×s	298.15	Densiti...
η	0.0019430	Pa×s	298.15	Excess ...
η	0.0021178	Pa×s	298.15	Density...
η	0.0018939	Pa×s	298.15	Densiti...
η	0.0019660	Pa×s	298.15	Densiti...
η	0.0019500	Pa×s	298.15	Densiti...
η	0.0019150	Pa×s	298.15	Dynamic...
η	0.0019150	Pa×s	298.15	Viscosi...
η	0.0020420	Pa×s	298.15	Viscosi...
η	0.0019550	Pa×s	298.15	Densiti...
η	0.0019810	Pa×s	298.15	Density...
η	0.0019760	Pa×s	298.15	Propert...
η	0.0019450	Pa×s	298.15	Viscosi...
η	0.0019730	Pa×s	298.15	Densiti...
η	0.0019414	Pa×s	298.15	Densiti...
η	0.0016100	Pa×s	303.00	Ultraso...
η	0.0017140	Pa×s	303.15	Viscosi...
η	0.0017282	Pa×s	303.15	Densiti...
η	0.0016145	Pa×s	303.15	Thermod...
η	0.0017260	Pa×s	303.15	Densiti...
η	0.0017450	Pa×s	303.15	Density...
η	0.0017250	Pa×s	303.15	Excess ...
η	0.0017370	Pa×s	303.15	Propert...
η	0.0017370	Pa×s	303.15	Densiti...
η	0.0018742	Pa×s	303.15	Density...
η	0.0017325	Pa×s	303.15	Densiti...
η	0.0017330	Pa×s	303.15	Densiti...
η	0.0017880	Pa×s	303.15	Densiti...
η	0.0017190	Pa×s	303.15	Densiti...
η	0.0017130	Pa×s	303.15	Viscosi...
η	0.0016841	Pa×s	303.15	Densiti...
η	0.0017300	Pa×s	303.15	Viscosi...
η	0.0017130	Pa×s	303.15	Density...
η	0.0017130	Pa×s	303.15	Dynamic...
η	0.0015380	Pa×s	308.15	Densiti...
η	0.0015037	Pa×s	308.15	Densiti...
η	0.0015448	Pa×s	308.15	Densiti...
η	0.0015330	Pa×s	308.15	Densiti...
η	0.0015344	Pa×s	308.15	Densiti...
η	0.0016709	Pa×s	308.15	Density...
η	0.0015400	Pa×s	308.15	Tempera...
η	0.0015480	Pa×s	308.15	Propert...
η	0.0015650	Pa×s	308.15	Viscosi...
η	0.0015370	Pa×s	308.15	Excess ...
η	0.0015480	Pa×s	308.15	Densiti...
η	0.0013400	Pa×s	313.00	Ultraso...
η	0.0013840	Pa×s	313.15	Densiti...
η	0.0013810	Pa×s	313.15	Densiti...
η	0.0013516	Pa×s	313.15	Densiti...
η	0.0011883	Pa×s	313.15	Thermod...
η	0.0013672	Pa×s	313.15	Densiti...
η	0.0013847	Pa×s	313.15	Densiti...
η	0.0013830	Pa×s	313.15	Propert...
η	0.0013907	Pa×s	313.15	Densiti...
η	0.0013730	Pa×s	313.15	Densiti...
η	0.0013780	Pa×s	313.15	Density...
η	0.0013630	Pa×s	313.15	Densiti...
η	0.0015237	Pa×s	313.15	Density...
η	0.0013820	Pa×s	313.15	Viscosi...
η	0.0013810	Pa×s	313.15	Density...
η	0.0012410	Pa×s	318.15	Densiti...
η	0.0012340	Pa×s	318.15	Densiti...
η	0.0013833	Pa×s	318.15	Density...
η	0.0012240	Pa×s	318.15	Densiti...
η	0.0012400	Pa×s	318.15	Tempera...
η	0.0008796	Pa×s	323.15	Thermod...
η	0.0012560	Pa×s	323.15	Density...
η	0.0011050	Pa×s	323.15	Viscosi...
η	0.0011150	Pa×s	323.15	Density...
η	0.0011170	Pa×s	323.15	Densiti...
η	0.0011004	Pa×s	323.15	Densiti...
η	0.0011020	Pa×s	323.15	Densiti...
η	0.0010977	Pa×s	323.15	Densiti...
η	0.0010200	Pa×s	328.15	Tempera...
η	0.0011523	Pa×s	328.15	Density...
η	0.0009860	Pa×s	328.15	Densiti...
η	0.0009070	Pa×s	333.15	Density...
η	0.0008980	Pa×s	333.15	Densiti...
η	0.0010819	Pa×s	333.15	Density...
η	0.0005985	Pa×s	333.15	Thermod...
η	0.0008420	Pa×s	338.15	Tempera...
η	0.0008010	Pa×s	338.15	Densiti...
η	0.0007420	Pa×s	343.15	Density...
η	0.0007100	Pa×s	348.15	Tempera...
η	0.0006150	Pa×s	353.15	Density...
η	0.0005150	Pa×s	363.15	Density...
ΔfusH	[5.19; 5.40]	kJ/mol	[147.00; 148.80]
ΔfusH	5.19	kJ/mol	147.00	NIST
ΔfusH	5.40	kJ/mol	148.70	NIST
ΔfusH	5.37	kJ/mol	148.75	NIST
ΔfusH	5.37	kJ/mol	148.80	NIST
ΔfusH	5.37	kJ/mol	148.80	NIST
ΔvapH	[11.40; 49.30]	kJ/mol	[214.00; 528.00]
ΔvapH	48.00	kJ/mol	214.00	NIST
ΔvapH	46.40 ± 0.10	kJ/mol	313.00	NIST
ΔvapH	46.70	kJ/mol	318.00	NIST
ΔvapH	45.70 ± 0.10	kJ/mol	323.00	NIST
ΔvapH	49.30	kJ/mol	324.00	NIST
ΔvapH	46.90	kJ/mol	331.00	NIST
ΔvapH	44.90 ± 0.10	kJ/mol	333.00	NIST
ΔvapH	44.99 ± 0.42	kJ/mol	333.13	NIST
ΔvapH	47.00	kJ/mol	336.50	NIST
ΔvapH	43.90 ± 0.10	kJ/mol	343.00	NIST
ΔvapH	44.00 ± 0.10	kJ/mol	343.00	NIST
ΔvapH	45.50	kJ/mol	344.00	NIST
ΔvapH	43.20 ± 0.10	kJ/mol	353.00	NIST
ΔvapH	43.20	kJ/mol	354.00	NIST
ΔvapH	44.70	kJ/mol	355.00	NIST
ΔvapH	44.30	kJ/mol	358.00	NIST
ΔvapH	42.30 ± 0.10	kJ/mol	360.00	NIST
ΔvapH	42.40 ± 0.10	kJ/mol	363.00	NIST
ΔvapH	44.10	kJ/mol	364.00	NIST
ΔvapH	43.50	kJ/mol	366.00	NIST
ΔvapH	42.90	kJ/mol	368.50	NIST
ΔvapH	41.20 ± 0.10	kJ/mol	370.00	NIST
ΔvapH	41.44	kJ/mol	370.30	NIST
ΔvapH	41.76	kJ/mol	370.40	KDB
ΔvapH	41.20	kJ/mol	371.00	NIST
ΔvapH	40.30 ± 0.10	kJ/mol	378.00	NIST
ΔvapH	39.70 ± 0.10	kJ/mol	384.00	NIST
ΔvapH	42.30	kJ/mol	388.00	NIST
ΔvapH	35.20	kJ/mol	423.00	NIST
ΔvapH	40.10	kJ/mol	441.50	NIST
ΔvapH	29.40	kJ/mol	453.00	NIST
ΔvapH	40.70	kJ/mol	471.00	NIST
ΔvapH	36.50	kJ/mol	492.50	NIST
ΔvapH	21.00	kJ/mol	498.00	NIST
ΔvapH	11.40	kJ/mol	528.00	NIST
Pvap	[0.70; 3546.00]	kPa	[278.15; 513.15]
Pvap	0.70	kPa	278.15	Vapor P...
Pvap	1.01	kPa	283.15	Vapor P...
Pvap	1.45	kPa	288.15	Vapor P...
Pvap	2.04	kPa	293.15	Vapor P...
Pvap	2.03	kPa	293.15	Thermod...
Pvap	2.88	kPa	298.15	Vapor-P...
Pvap	2.84	kPa	298.15	Vapor P...
Pvap	2.81	kPa	298.15	Thermod...
Pvap	2.79	kPa	298.15	Thermod...
Pvap	3.83	kPa	303.15	Thermod...
Pvap	4.00	kPa	303.15	Vapor-P...
Pvap	3.87	kPa	303.15	Vapor P...
Pvap	3.88	kPa	303.15	Thermod...
Pvap	3.63	kPa	303.15	Isother...
Pvap	5.23	kPa	308.15	Vapor P...
Pvap	5.25	kPa	308.15	Thermod...
Pvap	5.37	kPa	308.15	Vapor-P...
Pvap	5.20	kPa	308.15	Thermod...
Pvap	5.88	kPa	310.17	Vapor-L...
Pvap	6.99	kPa	313.15	Thermod...
Pvap	7.03	kPa	313.15	Thermod...
Pvap	7.01	kPa	313.15	Vapor P...
Pvap	6.98	kPa	313.15	Vapor-L...
Pvap	7.20	kPa	313.15	Vapor-P...
Pvap	6.99	kPa	313.17	P-x dat...
Pvap	7.69	kPa	314.84	Vapor-L...
Pvap	9.57	kPa	318.15	Vapor-P...
Pvap	9.01	kPa	318.15	Isother...
Pvap	9.29	kPa	318.15	Vapor P...
Pvap	9.31	kPa	318.15	Thermod...
Pvap	9.47	kPa	318.58	Vapor-L...
Pvap	10.00	kPa	319.65	P, rho,...
Pvap	10.18	kPa	319.89	Vapor-L...
Pvap	12.07	kPa	323.07	Vapor-L...
Pvap	12.18	kPa	323.15	Vapor P...
Pvap	12.32	kPa	323.15	Vapor-L...
Pvap	12.42	kPa	323.15	Vapor-P...
Pvap	12.27	kPa	323.26	Vapor-L...
Pvap	13.14	kPa	324.71	Vapor-L...
Pvap	15.00	kPa	327.25	P, rho,...
Pvap	15.75	kPa	328.14	Vapor-L...
Pvap	16.14	kPa	328.15	Vapor-P...
Pvap	17.57	kPa	330.16	Vapor-L...
Pvap	19.07	kPa	331.92	Vapor-L...
Pvap	19.17	kPa	332.05	Vapor-L...
Pvap	19.31	kPa	332.18	Vapor-L...
Pvap	20.00	kPa	332.95	P, rho,...
Pvap	20.72	kPa	333.15	Vapor-P...
Pvap	19.93	kPa	333.15	Isother...
Pvap	20.27	kPa	333.15	Vapor-L...
Pvap	21.90	kPa	334.53	Phase e...
Pvap	22.56	kPa	335.34	Vapor-L...
Pvap	25.00	kPa	337.45	P, rho,...
Pvap	25.60	kPa	337.95	Isobari...
Pvap	26.41	kPa	338.15	Vapor-P...
Pvap	26.91	kPa	339.01	Vapor-L...
Pvap	30.00	kPa	341.25	P, rho,...
Pvap	30.10	kPa	341.35	Isobari...
Pvap	31.20	kPa	342.07	Phase e...
Pvap	31.12	kPa	342.11	Vapor-L...
Pvap	31.45	kPa	342.83	P-x dat...
Pvap	33.23	kPa	343.15	Vapor-P...
Pvap	33.33	kPa	343.55	P, rho,...
Pvap	35.00	kPa	344.65	P, rho,...
Pvap	35.82	kPa	345.18	Vapor-L...
Pvap	37.40	kPa	346.15	Isobari...
Pvap	40.00	kPa	347.55	Isobari...
Pvap	40.00	kPa	347.65	P, rho,...
Pvap	40.12	kPa	347.71	Vapor-L...
Pvap	41.63	kPa	348.15	Vapor-P...
Pvap	42.90	kPa	349.12	Phase e...
Pvap	44.26	kPa	349.93	Vapor-L...
Pvap	45.00	kPa	350.35	P, rho,...
Pvap	46.00	kPa	350.80	Isobari...
Pvap	49.36	kPa	352.44	Vapor-L...
Pvap	49.80	kPa	352.68	P-x dat...
Pvap	50.00	kPa	352.75	P, rho,...
Pvap	51.67	kPa	353.15	Vapor-P...
Pvap	50.95	kPa	353.15	Vapor-L...
Pvap	50.95	kPa	353.17	Vapor-L...
Pvap	51.10	kPa	353.25	Isobari...
Pvap	52.70	kPa	353.96	Phase e...
Pvap	53.33	kPa	354.18	Isobari...
Pvap	55.00	kPa	355.05	P, rho,...
Pvap	59.13	kPa	356.70	Vapor-L...
Pvap	60.00	kPa	357.05	P, rho,...
Pvap	60.00	kPa	357.10	Isobari...
Pvap	60.70	kPa	357.35	Isobari...
Pvap	62.40	kPa	357.95	Phase e...
Pvap	63.69	kPa	358.15	Vapor-P...
Pvap	65.00	kPa	359.05	P, rho,...
Pvap	66.66	kPa	359.56	Isobari...
Pvap	66.66	kPa	359.65	P, rho,...
Pvap	70.00	kPa	360.85	P, rho,...
Pvap	71.40	kPa	361.25	Phase e...
Pvap	74.70	kPa	362.45	Isobari...
Pvap	75.00	kPa	362.55	P, rho,...
Pvap	77.81	kPa	363.15	Vapor-P...
Pvap	76.56	kPa	363.20	(Vapour...
Pvap	79.99	kPa	364.11	Isobari...
Pvap	80.00	kPa	364.15	P, rho,...
Pvap	80.00	kPa	364.20	Isobari...
Pvap	80.70	kPa	364.30	Phase e...
Pvap	81.30	kPa	364.51	Isother...
Pvap	81.20	kPa	364.53	Vapor L...
Pvap	85.00	kPa	365.65	P, rho,...
Pvap	86.80	kPa	366.25	Isobari...
Pvap	90.00	kPa	367.15	P, rho,...
Pvap	91.60	kPa	367.51	Phase e...
Pvap	93.32	kPa	368.08	Isobari...
Pvap	98.66	kPa	369.55	Isobari...
Pvap	100.00	kPa	369.80	Isobari...
Pvap	100.00	kPa	370.00	Isobari...
Pvap	101.33	kPa	370.05	P, rho,...
Pvap	100.51	kPa	370.10	Vapor-L...
Pvap	101.00	kPa	370.20	Heterog...
Pvap	101.30	kPa	370.33	Isobari...
Pvap	101.30	kPa	370.35	Isobari...
Pvap	101.30	kPa	370.40	Evaluat...
Pvap	101.80	kPa	370.40	Isobari...
Pvap	102.70	kPa	370.44	Phase e...
Pvap	114.90	kPa	373.65	Isobari...
Pvap	125.86	kPa	376.30	Vapor-L...
Pvap	151.03	kPa	381.50	Vapor-L...
Pvap	160.40	kPa	383.20	High-te...
Pvap	176.20	kPa	385.89	Vapor-L...
Pvap	201.37	kPa	389.89	Vapor-L...
Pvap	223.30	kPa	393.20	High-te...
Pvap	226.54	kPa	393.59	Vapor-L...
Pvap	251.71	kPa	396.19	Vapor-L...
Pvap	303.10	kPa	403.20	High-te...
Pvap	406.60	kPa	413.20	High-te...
Pvap	546.10	kPa	423.20	High-te...
Pvap	600.00	kPa	427.20	Experim...
Pvap	1558.00	kPa	468.15	Vapor-L...
Pvap	2081.00	kPa	483.15	Vapor-L...
Pvap	2733.00	kPa	498.15	Vapor-L...
Pvap	3546.00	kPa	513.15	Vapor-L...
n0	[1.37015; 1.38906]		[283.15; 328.15]
n0	1.38906		283.15	Thermop...
n0	1.38780		288.15	Experim...
n0	1.38690		288.15	Excess ...
n0	1.38785		288.15	Experim...
n0	1.38578		293.15	Experim...
n0	1.38500		293.15	Phase e...
n0	1.38480		293.15	Isother...
n0	1.38512		293.15	Vapor L...
n0	1.38550		293.15	Limitin...
n0	1.38530		293.15	Isother...
n0	1.38520		293.15	Solid-L...
n0	1.38432		293.15	Separat...
n0	1.38552		293.15	Excess ...
n0	1.38520		293.15	P-rho-T...
n0	1.38576		293.15	Experim...
n0	1.38510		293.15	Isobari...
n0	1.38200		293.15	Isother...
n0	1.38540		293.15	Solubil...
n0	1.38510		293.15	Vapor L...
n0	1.38530		293.15	Measure...
n0	1.38510		293.20	Vapor L...
n0	1.38510		293.20	Vapor L...
n0	1.38540		295.15	Isobari...
n0	1.38340		298.00	Determi...
n0	1.38310		298.15	Physica...
n0	1.38307		298.15	Thermop...
n0	1.38260		298.15	Thermod...
n0	1.38309		298.15	Density...
n0	1.38288		298.15	Thermop...
n0	1.38305		298.15	Experim...
n0	1.38260		298.15	Thermod...
n0	1.38220		298.15	Applica...
n0	1.38307		298.15	Effect ...
n0	1.38360		298.15	Liquid ...
n0	1.38400		298.15	Physico...
n0	1.38340		298.15	Excess ...
n0	1.38290		298.15	Experim...
n0	1.38340		298.15	Density...
n0	1.38330		298.15	Isother...
n0	1.38305		298.15	Liquid ...
n0	1.38300		298.15	Excess ...
n0	1.38560		298.15	Isobari...
n0	1.38334		298.15	Densiti...
n0	1.38320		298.15	Excess ...
n0	1.38330		298.15	Excess ...
n0	1.38360		298.15	Phase E...
n0	1.38330		298.15	Propert...
n0	1.38370		298.15	Experim...
n0	1.38369		298.15	Experim...
n0	1.38312		298.15	Isother...
n0	1.38305		298.15	Isobari...
n0	1.38364		298.15	Experim...
n0	1.38360		298.15	Isobari...
n0	1.38330		298.15	Effect ...
n0	1.38302		298.15	Physica...
n0	1.38330		298.15	Excess ...
n0	1.38304		298.15	Density...
n0	1.38350		298.15	Molar e...
n0	1.38333		298.15	Vapor l...
n0	1.38370		298.15	(Vapor ...
n0	1.38286		298.15	Effect ...
n0	1.38360		298.15	Phase e...
n0	1.38310		298.15	Synthes...
n0	1.38360		298.15	Vapor l...
n0	1.38360		298.15	Isobari...
n0	1.38070		298.15	Bubble ...
n0	1.38370		298.15	Activit...
n0	1.38290		298.15	Excess ...
n0	1.38300		298.15	Density...
n0	1.38306		298.15	Effect ...
n0	1.38308		298.15	Isobari...
n0	1.38390		298.20	Vapor l...
n0	1.38350		298.20	Measure...
n0	1.38190		303.15	Physico...
n0	1.38080		303.15	Thermod...
n0	1.38153		303.15	Experim...
n0	1.38080		303.15	Thermod...
n0	1.38210		303.15	Experim...
n0	1.38131		303.15	Densiti...
n0	1.38162		303.15	Experim...
n0	1.37820		308.15	Thermod...
n0	1.38000		308.15	Physico...
n0	1.37918		308.15	Experim...
n0	1.37929		308.15	Experim...
n0	1.37926		308.15	Densiti...
n0	1.37820		308.15	Thermod...
n0	1.37890		308.15	Excess ...
n0	1.37674		313.15	Thermop...
n0	1.37660		313.15	Thermop...
n0	1.37722		313.15	Densiti...
n0	1.37695		313.15	Experim...
n0	1.37702		313.15	Experim...
n0	1.37469		318.15	Experim...
n0	1.37483		318.15	Experim...
n0	1.37231		323.15	Experim...
n0	1.37252		323.15	Experim...
n0	1.37015		328.15	Thermop...
ρl	[742.77; 815.98]	kg/m3	[278.15; 363.15]
ρl	815.60	kg/m3	278.15	Thermop...
ρl	815.46	kg/m3	278.15	Density...
ρl	815.98	kg/m3	278.15	Volumet...
ρl	815.52	kg/m3	278.15	Density...
ρl	815.55	kg/m3	278.15	Thermod...
ρl	811.54	kg/m3	283.15	Excess ...
ρl	811.48	kg/m3	283.15	Densiti...
ρl	811.57	kg/m3	283.15	Volumet...
ρl	811.60	kg/m3	283.15	Thermod...
ρl	811.60	kg/m3	283.15	Density...
ρl	807.70	kg/m3	288.15	Thermop...
ρl	807.54	kg/m3	288.15	Volumet...
ρl	807.75	kg/m3	288.15	Experim...
ρl	807.62	kg/m3	288.15	Volumet...
ρl	807.75	kg/m3	288.15	Volumet...
ρl	807.50	kg/m3	288.15	Mass de...
ρl	807.83	kg/m3	288.15	Measure...
ρl	807.55	kg/m3	288.15	Excess ...
ρl	807.30	kg/m3	288.15	Tempera...
ρl	807.54	kg/m3	288.15	Densiti...
ρl	807.51	kg/m3	288.15	The exc...
ρl	807.64	kg/m3	288.15	Thermod...
ρl	809.01	kg/m3	288.15	Excess ...
ρl	807.86	kg/m3	288.15	Densiti...
ρl	807.69	kg/m3	288.15	Influen...
ρl	807.55	kg/m3	288.15	Thermop...
ρl	807.63	kg/m3	288.15	Density...
ρl	807.90	kg/m3	288.15	Thermod...
ρl	803.50	kg/m3	293.00	Fluid-P...
ρl	804.00	kg/m3	293.00	KDB
ρl	803.50	kg/m3	293.00	Fluid-P...
ρl	800.03	kg/m3	293.15	Excess ...
ρl	803.77	kg/m3	293.15	Volumet...
ρl	803.53	kg/m3	293.15	Volume ...
ρl	803.70	kg/m3	293.15	Influen...
ρl	803.52	kg/m3	293.15	The exc...
ρl	803.59	kg/m3	293.15	Excess ...
ρl	804.97	kg/m3	293.15	Densiti...
ρl	803.70	kg/m3	293.15	Measure...
ρl	803.65	kg/m3	293.15	Densiti...
ρl	803.86	kg/m3	293.15	Densiti...
ρl	803.52	kg/m3	293.15	Measure...
ρl	803.30	kg/m3	293.15	Excess ...
ρl	803.58	kg/m3	293.15	Densiti...
ρl	803.63	kg/m3	293.15	Excess ...
ρl	803.67	kg/m3	293.15	Volumet...
ρl	804.00	kg/m3	293.15	Composi...
ρl	803.62	kg/m3	293.15	Thermod...
ρl	804.14	kg/m3	293.15	Molecul...
ρl	803.59	kg/m3	293.15	Volumet...
ρl	803.85	kg/m3	293.15	(Liquid...
ρl	803.52	kg/m3	293.15	Electro...
ρl	803.75	kg/m3	293.15	Propert...
ρl	803.63	kg/m3	293.15	Volumet...
ρl	803.77	kg/m3	293.15	Experim...
ρl	803.85	kg/m3	293.15	(Liquid...
ρl	803.60	kg/m3	293.15	Liquid ...
ρl	803.57	kg/m3	293.15	Density...
ρl	803.61	kg/m3	293.15	Densiti...
ρl	803.66	kg/m3	293.15	Thermod...
ρl	803.76	kg/m3	293.15	Intermo...
ρl	803.00	kg/m3	293.15	Density...
ρl	803.71	kg/m3	293.15	Densiti...
ρl	803.65	kg/m3	293.15	Density...
ρl	803.77	kg/m3	293.15	Volumet...
ρl	803.60	kg/m3	293.15	Three B...
ρl	803.50	kg/m3	293.15	Density...
ρl	803.56	kg/m3	293.15	Densiti...
ρl	803.92	kg/m3	293.15	Osmotic...
ρl	803.49	kg/m3	293.15	Densiti...
ρl	803.84	kg/m3	293.15	Volumet...
ρl	803.48	kg/m3	293.15	Speed o...
ρl	799.50	kg/m3	298.00	Fluid-P...
ρl	800.00	kg/m3	298.00	Compara...
ρl	799.50	kg/m3	298.00	Fluid-P...
ρl	801.01	kg/m3	298.15	Densiti...
ρl	799.45	kg/m3	298.15	Apparen...
ρl	799.40	kg/m3	298.15	Excess ...
ρl	799.53	kg/m3	298.15	Volume ...
ρl	799.75	kg/m3	298.15	Measure...
ρl	799.50	kg/m3	298.15	Dynamic...
ρl	799.67	kg/m3	298.15	Volumet...
ρl	799.60	kg/m3	298.15	Densiti...
ρl	799.71	kg/m3	298.15	Densiti...
ρl	799.40	kg/m3	298.15	Density...
ρl	800.97	kg/m3	298.15	Excess ...
ρl	799.59	kg/m3	298.15	Excess ...
ρl	799.60	kg/m3	298.15	Vapor-L...
ρl	799.65	kg/m3	298.15	Density...
ρl	799.87	kg/m3	298.15	Physica...
ρl	797.60	kg/m3	298.15	Volumet...
ρl	804.27	kg/m3	298.15	Phase E...
ρl	799.56	kg/m3	298.15	ACSExce...
ρl	799.66	kg/m3	298.15	Thermod...
ρl	799.52	kg/m3	298.15	Separat...
ρl	799.70	kg/m3	298.15	Excess ...
ρl	799.52	kg/m3	298.15	Effect ...
ρl	799.52	kg/m3	298.15	Extract...
ρl	799.40	kg/m3	298.15	Tempera...
ρl	800.13	kg/m3	298.15	Molecul...
ρl	799.78	kg/m3	298.15	Densiti...
ρl	799.67	kg/m3	298.15	Thermop...
ρl	799.50	kg/m3	298.15	Isobari...
ρl	799.56	kg/m3	298.15	A combi...
ρl	799.54	kg/m3	298.15	Volumet...
ρl	799.60	kg/m3	298.15	Bubble ...
ρl	799.71	kg/m3	298.15	Propert...
ρl	799.65	kg/m3	298.15	FT-IR s...
ρl	799.60	kg/m3	298.15	Measure...
ρl	799.74	kg/m3	298.15	(Vapor ...
ρl	799.56	kg/m3	298.15	Excess ...
ρl	799.56	kg/m3	298.15	Measure...
ρl	799.70	kg/m3	298.15	Solubil...
ρl	799.85	kg/m3	298.15	Volumet...
ρl	799.61	kg/m3	298.15	Experim...
ρl	800.06	kg/m3	298.15	Solid-l...
ρl	799.62	kg/m3	298.15	Thermod...
ρl	802.00	kg/m3	298.15	Isobari...
ρl	800.94	kg/m3	298.15	Volumet...
ρl	800.10	kg/m3	298.15	Composi...
ρl	799.50	kg/m3	298.15	Fully a...
ρl	799.69	kg/m3	298.15	Physica...
ρl	799.93	kg/m3	298.15	A syste...
ρl	799.59	kg/m3	298.15	Densiti...
ρl	799.52	kg/m3	298.15	Separat...
ρl	799.53	kg/m3	298.15	Mass de...
ρl	799.67	kg/m3	298.15	Densiti...
ρl	799.71	kg/m3	298.15	Measure...
ρl	799.62	kg/m3	298.15	Liquid ...
ρl	799.58	kg/m3	298.15	Excess ...
ρl	800.13	kg/m3	298.15	Thermod...
ρl	799.56	kg/m3	298.15	Thermop...
ρl	800.61	kg/m3	298.15	Isother...
ρl	799.70	kg/m3	298.15	Thermod...
ρl	799.96	kg/m3	298.15	Liquid ...
ρl	799.67	kg/m3	298.15	Thermod...
ρl	799.70	kg/m3	298.15	Thermop...
ρl	799.49	kg/m3	298.15	Densiti...
ρl	799.76	kg/m3	298.15	Volumet...
ρl	799.55	kg/m3	298.15	Density...
ρl	799.69	kg/m3	298.15	Influen...
ρl	799.96	kg/m3	298.15	Tempera...
ρl	801.08	kg/m3	298.15	Modifie...
ρl	799.51	kg/m3	298.15	The exc...
ρl	799.65	kg/m3	298.15	Excess ...
ρl	799.46	kg/m3	298.15	Thermop...
ρl	799.70	kg/m3	298.15	Thermod...
ρl	799.52	kg/m3	298.15	Densiti...
ρl	799.94	kg/m3	298.15	Liquid ...
ρl	799.98	kg/m3	298.15	Binary ...
ρl	799.62	kg/m3	298.15	Volumet...
ρl	799.75	kg/m3	298.15	Experim...
ρl	799.89	kg/m3	298.15	Binary ...
ρl	799.51	kg/m3	298.15	Fluid P...
ρl	797.81	kg/m3	298.15	Excess ...
ρl	799.60	kg/m3	298.15	Experim...
ρl	799.28	kg/m3	298.15	Topolog...
ρl	799.81	kg/m3	298.15	Densiti...
ρl	800.61	kg/m3	298.15	Binary ...
ρl	799.70	kg/m3	298.15	Solubil...
ρl	799.65	kg/m3	298.15	Thermod...
ρl	799.28	kg/m3	298.15	Topolog...
ρl	799.30	kg/m3	298.15	Thermod...
ρl	800.70	kg/m3	298.15	Apparen...
ρl	799.10	kg/m3	298.15	Excess ...
ρl	799.51	kg/m3	298.15	Excess ...
ρl	799.74	kg/m3	298.15	Densiti...
ρl	799.97	kg/m3	298.15	Excess ...
ρl	799.69	kg/m3	298.15	Volumet...
ρl	800.62	kg/m3	298.15	Speeds ...
ρl	800.00	kg/m3	298.15	Density...
ρl	799.52	kg/m3	298.15	Electro...
ρl	799.56	kg/m3	298.15	Refract...
ρl	799.47	kg/m3	298.15	Speed o...
ρl	799.92	kg/m3	298.20	A green...
ρl	796.00	kg/m3	303.00	Compara...
ρl	795.50	kg/m3	303.00	Fluid-P...
ρl	795.50	kg/m3	303.00	Fluid-P...
ρl	795.55	kg/m3	303.15	Excess ...
ρl	796.55	kg/m3	303.15	Isother...
ρl	796.89	kg/m3	303.15	Densiti...
ρl	795.72	kg/m3	303.15	Experim...
ρl	795.58	kg/m3	303.15	Volumet...
ρl	796.00	kg/m3	303.15	Density...
ρl	795.53	kg/m3	303.15	Vapor-l...
ρl	795.65	kg/m3	303.15	Influen...
ρl	795.72	kg/m3	303.15	Volumet...
ρl	795.82	kg/m3	303.15	Intermo...
ρl	795.48	kg/m3	303.15	Excess ...
ρl	795.87	kg/m3	303.15	Densiti...
ρl	795.61	kg/m3	303.15	Volumet...
ρl	795.62	kg/m3	303.15	Thermod...
ρl	795.70	kg/m3	303.15	Measure...
ρl	795.47	kg/m3	303.15	Measure...
ρl	795.05	kg/m3	303.15	Excess ...
ρl	796.00	kg/m3	303.15	Composi...
ρl	795.89	kg/m3	303.15	A syste...
ρl	795.81	kg/m3	303.15	Volumet...
ρl	795.50	kg/m3	303.15	Electro...
ρl	795.53	kg/m3	303.15	Density...
ρl	795.57	kg/m3	303.15	Densiti...
ρl	795.50	kg/m3	303.15	Densiti...
ρl	795.53	kg/m3	303.15	Volumet...
ρl	795.58	kg/m3	303.15	Volumet...
ρl	796.40	kg/m3	303.15	Excess ...
ρl	795.10	kg/m3	303.15	Excess ...
ρl	795.49	kg/m3	303.15	Volume ...
ρl	795.70	kg/m3	303.15	Liquid ...
ρl	795.40	kg/m3	303.15	Density...
ρl	795.58	kg/m3	303.15	Densiti...
ρl	795.65	kg/m3	303.15	FT-IR s...
ρl	795.48	kg/m3	303.15	The exc...
ρl	795.61	kg/m3	303.15	Density...
ρl	795.94	kg/m3	303.15	Physica...
ρl	798.00	kg/m3	303.15	Study o...
ρl	795.92	kg/m3	303.15	Tempera...
ρl	796.08	kg/m3	303.15	Molecul...
ρl	795.80	kg/m3	303.15	Viscous...
ρl	795.58	kg/m3	303.15	Thermod...
ρl	795.54	kg/m3	303.15	Isobari...
ρl	795.77	kg/m3	303.15	Densiti...
ρl	795.58	kg/m3	303.15	Densiti...
ρl	795.46	kg/m3	303.15	Densiti...
ρl	795.65	kg/m3	303.15	Propert...
ρl	795.54	kg/m3	303.15	Densiti...
ρl	795.44	kg/m3	303.15	Speed o...
ρl	792.00	kg/m3	308.00	Compara...
ρl	791.58	kg/m3	308.15	Influen...
ρl	791.43	kg/m3	308.15	Volume ...
ρl	791.76	kg/m3	308.15	Thermod...
ρl	791.46	kg/m3	308.15	Thermop...
ρl	791.43	kg/m3	308.15	Electro...
ρl	791.80	kg/m3	308.15	Densiti...
ρl	791.83	kg/m3	308.15	Densiti...
ρl	791.69	kg/m3	308.15	Densiti...
ρl	791.55	kg/m3	308.15	Thermod...
ρl	791.30	kg/m3	308.15	Density...
ρl	791.74	kg/m3	308.15	Volumet...
ρl	791.39	kg/m3	308.15	Densiti...
ρl	791.60	kg/m3	308.15	Thermop...
ρl	791.53	kg/m3	308.15	Densiti...
ρl	791.36	kg/m3	308.15	Thermop...
ρl	791.30	kg/m3	308.15	Tempera...
ρl	791.44	kg/m3	308.15	Volumet...
ρl	791.84	kg/m3	308.15	Osmotic...
ρl	791.63	kg/m3	308.15	Measure...
ρl	791.71	kg/m3	308.15	Densiti...
ρl	791.49	kg/m3	308.15	Volumet...
ρl	791.82	kg/m3	308.15	Tempera...
ρl	791.64	kg/m3	308.15	Volumet...
ρl	791.52	kg/m3	308.15	Volumet...
ρl	791.82	kg/m3	308.15	A syste...
ρl	791.50	kg/m3	308.15	Densiti...
ρl	792.76	kg/m3	308.15	Physica...
ρl	791.64	kg/m3	308.15	Experim...
ρl	791.47	kg/m3	308.15	Excess ...
ρl	791.54	kg/m3	308.15	Density...
ρl	791.51	kg/m3	308.15	Thermod...
ρl	791.42	kg/m3	308.15	The exc...
ρl	791.65	kg/m3	308.15	FT-IR s...
ρl	791.56	kg/m3	308.15	Propert...
ρl	791.40	kg/m3	308.15	Measure...
ρl	791.44	kg/m3	308.15	Mass de...
ρl	792.83	kg/m3	308.15	Densiti...
ρl	791.78	kg/m3	308.15	Physica...
ρl	792.00	kg/m3	308.15	Molecul...
ρl	791.40	kg/m3	308.15	Vapor-L...
ρl	791.37	kg/m3	308.15	Speed o...
ρl	789.00	kg/m3	313.00	Compara...
ρl	787.30	kg/m3	313.15	Measure...
ρl	787.36	kg/m3	313.15	Excess ...
ρl	787.88	kg/m3	313.15	Molecul...
ρl	787.31	kg/m3	313.15	The exc...
ρl	787.42	kg/m3	313.15	Propert...
ρl	787.39	kg/m3	313.15	Densiti...
ρl	787.41	kg/m3	313.15	Thermod...
ρl	787.43	kg/m3	313.15	Density...
ρl	787.52	kg/m3	313.15	Measure...
ρl	787.35	kg/m3	313.15	Density...
ρl	788.00	kg/m3	313.15	Composi...
ρl	787.52	kg/m3	313.15	Volumet...
ρl	787.95	kg/m3	313.15	Excess ...
ρl	787.88	kg/m3	313.15	Intermo...
ρl	787.37	kg/m3	313.15	Volumet...
ρl	787.47	kg/m3	313.15	Influen...
ρl	788.00	kg/m3	313.15	Density...
ρl	787.73	kg/m3	313.15	Tempera...
ρl	787.38	kg/m3	313.15	Volumet...
ρl	787.44	kg/m3	313.15	Densiti...
ρl	788.69	kg/m3	313.15	Excess ...
ρl	787.20	kg/m3	313.15	Density...
ρl	789.07	kg/m3	313.15	Densiti...
ρl	787.29	kg/m3	313.15	Densiti...
ρl	787.30	kg/m3	313.15	Densiti...
ρl	787.83	kg/m3	313.15	Densiti...
ρl	787.50	kg/m3	313.15	Liquid ...
ρl	787.52	kg/m3	313.15	Experim...
ρl	787.32	kg/m3	313.15	Volume ...
ρl	787.36	kg/m3	313.15	Excess ...
ρl	787.00	kg/m3	313.15	Excess ...
ρl	787.64	kg/m3	313.15	Volumet...
ρl	788.60	kg/m3	313.15	Excess ...
ρl	787.31	kg/m3	313.15	Electro...
ρl	787.72	kg/m3	313.15	Densiti...
ρl	787.34	kg/m3	313.15	Densiti...
ρl	787.42	kg/m3	313.15	Volumet...
ρl	787.37	kg/m3	313.15	Densiti...
ρl	787.26	kg/m3	313.15	Speed o...
ρl	783.12	kg/m3	318.15	Measure...
ρl	783.16	kg/m3	318.15	Volume ...
ρl	783.30	kg/m3	318.15	Densiti...
ρl	783.36	kg/m3	318.15	Volumet...
ρl	783.10	kg/m3	318.15	Density...
ρl	783.12	kg/m3	318.15	Vapor-L...
ρl	783.27	kg/m3	318.15	Density...
ρl	783.15	kg/m3	318.15	The exc...
ρl	783.64	kg/m3	318.15	Densiti...
ρl	783.17	kg/m3	318.15	Volumet...
ρl	783.11	kg/m3	318.15	Electro...
ρl	783.36	kg/m3	318.15	Measure...
ρl	783.56	kg/m3	318.15	Densiti...
ρl	783.18	kg/m3	318.15	Density...
ρl	784.45	kg/m3	318.15	Physica...
ρl	783.22	kg/m3	318.15	Volumet...
ρl	783.10	kg/m3	318.15	Thermop...
ρl	783.30	kg/m3	318.15	Thermop...
ρl	783.16	kg/m3	318.15	Thermod...
ρl	783.22	kg/m3	318.15	Volumet...
ρl	783.86	kg/m3	318.15	Densiti...
ρl	783.30	kg/m3	318.15	Densiti...
ρl	783.20	kg/m3	318.15	Thermop...
ρl	783.20	kg/m3	318.15	Excess ...
ρl	783.18	kg/m3	318.15	Mass de...
ρl	783.36	kg/m3	318.15	Experim...
ρl	783.55	kg/m3	318.15	Volumet...
ρl	783.14	kg/m3	318.15	Densiti...
ρl	783.10	kg/m3	318.15	Speed o...
ρl	779.14	kg/m3	323.15	Volumet...
ρl	778.98	kg/m3	323.15	Density...
ρl	780.00	kg/m3	323.15	Composi...
ρl	779.11	kg/m3	323.15	Densiti...
ρl	779.14	kg/m3	323.15	Measure...
ρl	779.30	kg/m3	323.15	Liquid-...
ρl	779.02	kg/m3	323.15	Densiti...
ρl	779.01	kg/m3	323.15	Densiti...
ρl	778.92	kg/m3	323.15	Volumet...
ρl	779.01	kg/m3	323.15	Volumet...
ρl	780.74	kg/m3	323.15	Densiti...
ρl	778.93	kg/m3	323.15	Densiti...
ρl	779.33	kg/m3	323.15	Osmotic...
ρl	779.09	kg/m3	323.15	Osmotic...
ρl	779.05	kg/m3	323.15	Density...
ρl	778.79	kg/m3	323.15	Electro...
ρl	779.00	kg/m3	323.15	Densiti...
ρl	779.14	kg/m3	323.15	Experim...
ρl	778.97	kg/m3	323.15	Densiti...
ρl	778.93	kg/m3	323.15	Measure...
ρl	779.36	kg/m3	323.15	Densiti...
ρl	779.20	kg/m3	323.15	Liquid ...
ρl	778.70	kg/m3	323.15	Excess ...
ρl	778.90	kg/m3	323.15	Density...
ρl	778.96	kg/m3	323.15	Volumet...
ρl	779.09	kg/m3	323.15	Vapor-l...
ρl	779.32	kg/m3	323.15	Volumet...
ρl	780.00	kg/m3	323.15	Density...
ρl	778.90	kg/m3	323.15	Speed o...
ρl	774.90	kg/m3	328.15	Densiti...
ρl	774.70	kg/m3	328.15	Mass de...
ρl	774.63	kg/m3	328.15	Thermop...
ρl	774.86	kg/m3	328.15	Densiti...
ρl	774.73	kg/m3	328.15	Volumet...
ρl	775.97	kg/m3	328.15	Excess ...
ρl	774.72	kg/m3	328.15	Thermop...
ρl	774.90	kg/m3	328.15	Thermop...
ρl	774.79	kg/m3	328.15	Density...
ρl	770.54	kg/m3	333.15	Densiti...
ρl	770.39	kg/m3	333.15	Volumet...
ρl	770.44	kg/m3	333.15	Density...
ρl	770.38	kg/m3	333.15	Density...
ρl	771.75	kg/m3	333.15	Densiti...
ρl	764.00	kg/m3	333.15	Composi...
ρl	770.80	kg/m3	333.15	Densiti...
ρl	770.42	kg/m3	333.15	Densiti...
ρl	770.32	kg/m3	333.15	Measure...
ρl	770.42	kg/m3	333.15	Densiti...
ρl	765.98	kg/m3	338.15	Thermop...
ρl	766.20	kg/m3	338.15	Thermop...
ρl	765.96	kg/m3	338.15	Density...
ρl	766.03	kg/m3	338.15	Density...
ρl	766.15	kg/m3	338.15	Densiti...
ρl	761.51	kg/m3	343.15	Densiti...
ρl	761.53	kg/m3	343.15	Density...
ρl	761.67	kg/m3	343.15	Densiti...
ρl	762.86	kg/m3	343.15	Densiti...
ρl	756.91	kg/m3	348.15	Thermop...
ρl	757.09	kg/m3	348.15	Densiti...
ρl	752.44	kg/m3	353.15	Densiti...
ρl	747.65	kg/m3	358.15	Densiti...
ρl	742.77	kg/m3	363.15	Densiti...
ΔfusS	[35.30; 36.11]	J/mol×K	[147.00; 148.75]
ΔfusS	35.30	J/mol×K	147.00	NIST
ΔfusS	36.11	J/mol×K	148.75	NIST
csound,fluid	[1070.97; 1275.27]	m/s	[278.15; 338.15]
csound,fluid	1275.27	m/s	278.15	Volumet...
csound,fluid	1257.90	m/s	283.15	Excess ...
csound,fluid	1240.01	m/s	288.15	Densiti...
csound,fluid	1239.86	m/s	288.15	Volumet...
csound,fluid	1223.40	m/s	293.15	Acousti...
csound,fluid	1223.17	m/s	293.15	Densiti...
csound,fluid	1206.47	m/s	298.15	Densiti...
csound,fluid	1205.80	m/s	298.15	Ultraso...
csound,fluid	1207.00	m/s	298.15	Compres...
csound,fluid	1205.37	m/s	298.15	Volumet...
csound,fluid	1206.00	m/s	298.15	Excess ...
csound,fluid	1189.86	m/s	303.15	Densiti...
csound,fluid	1172.30	m/s	308.15	Acousti...
csound,fluid	1172.04	m/s	308.15	Densiti...
csound,fluid	1171.41	m/s	308.15	Volumet...
csound,fluid	1155.10	m/s	313.15	Excess ...
csound,fluid	1137.83	m/s	318.15	Volumet...
csound,fluid	1121.80	m/s	323.15	Acousti...
csound,fluid	1104.40	m/s	328.15	Volumet...
csound,fluid	1070.97	m/s	338.15	Volumet...
γ	[0.02; 0.02]	N/m	[278.15; 333.20]
γ	0.02	N/m	278.15	Applica...
γ	0.02	N/m	283.15	Applica...
γ	0.02	N/m	288.15	Surface...
γ	0.02	N/m	288.15	Applica...
γ	0.02	N/m	288.15	Study o...
γ	0.02	N/m	288.15	The mol...
γ	0.02	N/m	293.15	Surface...
γ	0.02	N/m	293.15	Density...
γ	0.02	N/m	293.15	The mol...
γ	0.02	N/m	293.15	Applica...
γ	0.02	N/m	293.20	Surface...
γ	0.02	N/m	293.20	KDB
γ	0.02	N/m	298.00	Surface...
γ	0.02	N/m	298.15	Surface...
γ	0.02	N/m	298.15	Study o...
γ	0.02	N/m	298.15	Applica...
γ	0.02	N/m	298.15	The mol...
γ	0.02	N/m	298.15	Surface...
γ	0.02	N/m	298.15	Surface...
γ	0.02	N/m	303.15	Applica...
γ	0.02	N/m	303.15	Surface...
γ	0.02	N/m	303.15	The mol...
γ	0.02	N/m	303.15	Surface...
γ	0.02	N/m	303.20	Surface...
γ	0.02	N/m	308.15	Surface...
γ	0.02	N/m	308.15	Applica...
γ	0.02	N/m	308.15	The mol...
γ	0.02	N/m	308.15	Surface...
γ	0.02	N/m	308.15	Study o...
γ	0.02	N/m	308.15	Surface...
γ	0.02	N/m	313.15	The mol...
γ	0.02	N/m	313.15	Applica...
γ	0.02	N/m	313.15	Surface...
γ	0.02	N/m	313.15	Surface...
γ	0.02	N/m	313.20	Surface...
γ	0.02	N/m	318.15	Surface...
γ	0.02	N/m	318.15	The mol...
γ	0.02	N/m	318.15	Surface...
γ	0.02	N/m	318.15	Study o...
γ	0.02	N/m	318.15	Surface...
γ	0.02	N/m	323.15	Surface...
γ	0.02	N/m	323.15	Surface...
γ	0.02	N/m	323.20	Surface...
γ	0.02	N/m	328.15	Study o...
γ	0.02	N/m	333.20	Surface...

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboil	[360.86; 423.16]	K	[69.79; 561.50]
Tboil	360.86	K	69.79	A novel...
Tboil	362.60	K	74.92	A novel...
Tboil	364.11	K	79.60	A novel...
Tboil	365.70	K	84.80	A novel...
Tboil	367.14	K	89.78	A novel...
Tboil	368.52	K	94.77	A novel...
Tboil	369.82	K	99.70	A novel...
Tboil	371.30	K	105.14	A novel...
Tboil	372.42	K	110.10	A novel...
Tboil	373.15	K	113.19	A novel...
Tboil	374.88	K	120.75	A novel...
Tboil	376.91	K	130.10	A novel...
Tboil	384.57	K	171.00	A novel...
Tboil	389.14	K	199.90	A novel...
Tboil	393.15	K	228.50	A novel...
Tboil	393.35	K	229.90	A novel...
Tboil	397.13	K	260.00	A novel...
Tboil	400.57	K	290.00	A novel...
Tboil	402.71	K	310.00	A novel...
Tboil	404.74	K	330.00	A novel...
Tboil	406.69	K	350.00	A novel...
Tboil	409.43	K	380.00	A novel...
Tboil	411.18	K	400.00	A novel...
Tboil	412.84	K	420.00	A novel...
Tboil	415.23	K	450.00	A novel...
Tboil	417.52	K	480.00	A novel...
Tboil	418.96	K	500.00	A novel...
Tboil	420.37	K	520.00	A novel...
Tboil	421.06	K	530.00	A novel...
Tboil	422.41	K	550.00	A novel...
Tboil	423.16	K	561.50	A novel...

Datasets

1. Molar heat capacity at constant volume, J/K/mol (1)
2. Viscosity, Pa*s (2)
3. Refractive index (Na D-line) (2)
4. Mass density, kg/m3 (12)
5. Speed of sound, m/s (3)
6. Molar volume, m3/mol (1)

Molar heat capacity at constant volume, J/K/mol

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Molar heat capacity at constant volume, J/K/mol - Liquid
314.15	4353.00	130.947
315.15	5217.00	131.0071
316.15	6081.00	131.7283
317.15	6946.00	132.6297
318.15	7808.00	133.2307
319.15	8666.00	133.2908
320.15	9526.00	133.6513
321.15	10392.00	134.6128
322.15	11260.00	134.9133
323.15	12130.00	135.8147
324.15	13000.00	135.8748
325.15	13871.00	136.3556
326.15	14740.00	137.4974
327.15	15599.00	136.9566
328.15	16461.00	139.1801
329.15	17326.00	138.519
330.15	18193.00	138.6993
331.15	19066.00	139.9012
332.15	19945.00	139.6007
333.15	20825.00	140.1416
334.15	21705.00	140.8026
335.15	22585.00	141.4637
336.15	23467.00	141.644
337.15	24350.00	141.2834
338.15	25234.00	142.5454
339.15	26119.00	142.7858
340.15	27006.00	143.7473
341.15	27893.00	143.0862
342.15	28774.00	145.0093
343.15	3874.00	148.615
343.15	29657.00	143.9276
344.15	4675.00	146.9924
345.15	5478.00	149.3361
346.15	6283.00	148.1943
347.15	7088.00	149.5164
348.15	7896.00	148.8554
349.15	8704.00	149.9972
350.15	9514.00	150.7784
351.15	10326.00	149.9972
352.15	11138.00	151.3193
353.15	11953.00	151.7399
354.15	12769.00	152.4611
355.15	13587.00	151.6798
356.15	14406.00	152.5813
357.15	15227.00	152.9418
358.15	16050.00	153.4827
359.15	16870.00	153.4226
360.15	17670.00	155.3456
361.15	18489.00	154.1437
362.15	19314.00	155.5259
363.15	20144.00	154.9851
364.15	20977.00	154.9851
365.15	21811.00	155.4057
366.15	22647.00	156.6677
367.15	23484.00	156.0067
368.15	24324.00	156.0668
369.15	25165.00	156.9682
370.15	26008.00	156.3071
371.15	26853.00	157.0884
372.15	2876.00	161.3551
372.15	27699.00	156.5475
373.15	3622.00	161.9561
373.15	28548.00	157.5691
374.15	4369.00	162.1965
374.15	29398.00	157.8095
375.15	5118.00	162.4969
376.15	5868.00	163.158
377.15	6620.00	163.158
378.15	7374.00	162.8575
379.15	8129.00	163.2181
380.15	8887.00	163.6387
381.15	9646.00	163.7589
382.15	10407.00	162.8575
383.15	11170.00	164.6003
384.15	11935.00	162.7373
385.15	12702.00	164.4801
386.15	13470.00	163.819
387.15	14240.00	164.2397
388.15	15013.00	164.1796
389.15	15786.00	164.2998
390.15	16562.00	164.2397
391.15	17338.00	164.8406
392.15	18116.00	163.4585
393.15	18896.00	164.3599
394.15	19677.00	164.2998
395.15	20459.00	164.3599
396.15	21244.00	164.5402
397.15	22030.00	164.6604
398.15	22817.00	164.7204
399.15	23606.00	164.8406
400.15	24395.00	163.9993
401.15	25186.00	164.3599
402.15	25978.00	164.2397
403.15	26772.00	163.7589
404.15	27566.00	163.819
405.15	28362.00	163.0979
406.15	29159.00	163.5786
414.15	10151.00	171.2708
415.15	10841.00	173.7948
416.15	11533.00	172.5929
417.15	12227.00	172.7732
418.15	12922.00	173.0737
419.15	13618.00	171.6314
420.15	14316.00	172.5328
421.15	15015.00	172.2924
422.15	15715.00	172.052
423.15	16417.00	172.3525
424.15	17119.00	172.4126
427.15	19232.00	172.1121
428.15	19938.00	171.4511
429.15	20645.00	171.4511
430.15	21353.00	172.052
Reference

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
298.15	81.50	0.0019
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Viscosity, Pa*s - Liquid
100.00	293.15	0.0022
100.00	313.15	0.0014
100.00	333.15	0.0009
100.00	353.15	0.0006
20000.00	293.15	0.0025
20000.00	313.15	0.0016
20000.00	333.15	0.0011
20000.00	353.15	0.0007
40000.00	293.15	0.0029
40000.00	313.15	0.0019
40000.00	333.15	0.0013
40000.00	353.15	0.0008
60000.00	293.15	0.0032
60000.00	313.15	0.0021
60000.00	333.15	0.0014
60000.00	353.15	0.0010
80000.00	293.15	0.0036
80000.00	313.15	0.0024
80000.00	333.15	0.0016
80000.00	353.15	0.0011
100000.00	293.15	0.0041
100000.00	313.15	0.0026
100000.00	333.15	0.0018
100000.00	353.15	0.0012
Reference

Refractive index (Na D-line)

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Refractive index (Na D-line) - Liquid
100.00	298.15	1.3836
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Refractive index (Na D-line) - Liquid
294.15	100.00	1.3846
Reference

Mass density, kg/m3

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
100.00	293.15	803.5
100.00	303.15	795.2
100.00	313.15	787.6
100.00	323.15	779.3
100.00	333.15	770.5
100.00	343.15	761.0
100.00	353.15	752.2
5000.00	293.15	807.3
5000.00	303.15	799.2
5000.00	313.15	791.9
5000.00	323.15	783.7
5000.00	333.15	775.4
5000.00	343.15	766.0
5000.00	353.15	757.6
10000.00	293.15	810.9
10000.00	303.15	802.9
10000.00	313.15	795.9
10000.00	323.15	788.0
10000.00	333.15	780.0
10000.00	343.15	770.7
10000.00	353.15	762.7
15000.00	293.15	814.3
15000.00	303.15	806.7
15000.00	313.15	799.7
15000.00	323.15	792.0
15000.00	333.15	784.3
15000.00	343.15	775.3
15000.00	353.15	767.6
20000.00	293.15	817.7
20000.00	303.15	810.1
20000.00	313.15	803.3
20000.00	323.15	795.8
20000.00	333.15	788.4
20000.00	343.15	779.6
20000.00	353.15	772.1
25000.00	293.15	821.0
25000.00	303.15	813.6
25000.00	313.15	806.8
25000.00	323.15	799.7
25000.00	333.15	792.0
25000.00	343.15	783.7
25000.00	353.15	776.3
30000.00	293.15	824.0
30000.00	303.15	816.7
30000.00	313.15	810.2
30000.00	323.15	803.2
30000.00	333.15	795.7
30000.00	343.15	787.6
30000.00	353.15	780.4
35000.00	293.15	827.0
35000.00	303.15	819.8
35000.00	313.15	813.5
35000.00	323.15	806.6
35000.00	333.15	799.2
35000.00	343.15	791.2
35000.00	353.15	784.1
40000.00	293.15	829.9
40000.00	303.15	822.9
40000.00	313.15	816.6
40000.00	323.15	809.9
40000.00	333.15	802.6
40000.00	343.15	794.7
40000.00	353.15	787.7
45000.00	293.15	832.7
45000.00	303.15	825.8
45000.00	313.15	819.7
45000.00	323.15	813.0
45000.00	333.15	805.9
45000.00	343.15	798.3
45000.00	353.15	791.8
50000.00	293.15	835.4
50000.00	303.15	828.8
50000.00	313.15	822.7
50000.00	323.15	816.1
50000.00	333.15	809.1
50000.00	343.15	801.6
50000.00	353.15	795.1
55000.00	293.15	838.1
55000.00	303.15	831.6
55000.00	313.15	825.5
55000.00	323.15	819.0
55000.00	333.15	812.3
55000.00	343.15	804.6
55000.00	353.15	798.5
60000.00	293.15	840.7
60000.00	303.15	834.2
60000.00	313.15	828.3
60000.00	323.15	821.8
60000.00	333.15	815.2
60000.00	343.15	807.7
60000.00	353.15	801.7
65000.00	293.15	843.2
65000.00	303.15	837.0
65000.00	313.15	831.0
65000.00	323.15	824.6
65000.00	333.15	818.1
65000.00	343.15	810.6
65000.00	353.15	805.0
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	110.00	799.54
298.15	5270.00	803.6
298.15	9870.00	807.01
298.15	14700.00	810.46
298.15	20530.00	814.46
298.15	25030.00	817.44
298.15	30100.00	820.7
298.15	35010.00	823.76
298.15	39560.00	826.52
323.15	590.00	779.78
323.15	5940.00	784.71
323.15	10600.00	788.81
323.15	16000.00	793.2
323.15	20640.00	796.73
323.15	24880.00	799.83
323.15	30800.00	803.99
323.15	35220.00	807.01
323.15	39790.00	810.02
348.15	140.00	757.11
348.15	5170.00	762.68
348.15	10260.00	767.5
348.15	15790.00	772.52
348.15	20560.00	776.41
348.15	24810.00	780.32
348.15	29300.00	784.09
348.15	35560.00	789.01
348.15	39950.00	792.23
373.15	360.00	733.24
373.15	5480.00	739.29
373.15	10290.00	745.11
373.15	15700.00	750.9
373.15	19960.00	755.19
373.15	25170.00	760.17
373.15	30510.00	765.02
373.15	35920.00	769.7
373.15	39780.00	772.91
398.15	620.00	705.55
398.15	5670.00	713.23
398.15	10620.00	720.1
398.15	15580.00	726.46
398.15	20350.00	732.35
398.15	25090.00	737.77
398.15	31150.00	744.07
398.15	35410.00	748.41
398.15	39390.00	752.32
423.15	1570.00	674.63
423.15	5870.00	682.79
423.15	10160.00	690.93
423.15	15320.00	699.32
423.15	20500.00	707.2
423.15	26280.00	715.01
423.15	31600.00	721.36
423.15	35780.00	726.03
423.15	39700.00	730.17
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.15	100.00	803.8
293.15	10000.00	811.3
293.15	20000.00	818.1
293.15	30000.00	824.4
293.15	40000.00	830.0
293.15	50000.00	835.6
293.15	60000.00	841.0
293.15	70000.00	845.9
293.15	80000.00	850.7
293.15	90000.00	855.2
293.15	100000.00	859.6
293.15	110000.00	863.7
293.15	120000.00	867.8
293.15	130000.00	871.6
293.15	140000.00	875.3
313.15	100.00	787.1
313.15	10000.00	795.5
313.15	20000.00	803.0
313.15	30000.00	810.0
313.15	40000.00	816.4
313.15	50000.00	822.3
313.15	60000.00	827.9
313.15	70000.00	833.2
313.15	80000.00	838.3
313.15	90000.00	843.0
313.15	100000.00	847.9
313.15	110000.00	852.3
313.15	120000.00	856.6
313.15	130000.00	860.7
313.15	140000.00	864.6
333.15	100.00	769.9
333.15	10000.00	780.0
333.15	20000.00	788.3
333.15	30000.00	795.7
333.15	40000.00	802.5
333.15	50000.00	809.0
333.15	60000.00	815.0
333.15	70000.00	820.6
333.15	80000.00	826.2
333.15	90000.00	831.2
333.15	100000.00	836.3
333.15	110000.00	840.9
333.15	120000.00	845.3
333.15	130000.00	849.6
333.15	140000.00	853.6
353.15	100.00	752.0
353.15	10000.00	762.5
353.15	20000.00	771.8
353.15	30000.00	780.2
353.15	40000.00	787.9
353.15	50000.00	795.0
353.15	60000.00	801.4
353.15	70000.00	807.7
353.15	80000.00	813.4
353.15	90000.00	818.7
353.15	100000.00	823.8
353.15	110000.00	828.8
353.15	120000.00	833.5
353.15	130000.00	837.9
353.15	140000.00	842.1
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
278.15	100.00	815.7
278.15	1000.00	816.4
278.15	5000.00	819.4
278.15	10000.00	822.8
278.15	15000.00	826.2
278.15	20000.00	829.4
278.15	25000.00	832.6
278.15	30000.00	835.7
278.15	35000.00	838.6
278.15	40000.00	841.5
278.15	45000.00	844.3
278.15	50000.00	847.1
278.15	55000.00	849.7
278.15	60000.00	852.1
288.15	100.00	807.8
288.15	1000.00	808.5
288.15	5000.00	811.6
288.15	10000.00	815.3
288.15	15000.00	818.9
288.15	20000.00	822.3
288.15	25000.00	825.5
288.15	30000.00	828.7
288.15	35000.00	831.8
288.15	40000.00	834.7
288.15	45000.00	837.6
288.15	50000.00	840.4
288.15	55000.00	843.1
288.15	60000.00	845.6
298.15	100.00	799.8
298.15	1000.00	800.5
298.15	5000.00	803.8
298.15	10000.00	807.6
298.15	15000.00	811.4
298.15	20000.00	814.9
298.15	25000.00	818.3
298.15	30000.00	821.6
298.15	35000.00	824.8
298.15	40000.00	827.9
298.15	45000.00	830.9
298.15	50000.00	833.8
298.15	55000.00	836.6
298.15	60000.00	839.2
308.15	100.00	791.6
308.15	1000.00	792.4
308.15	5000.00	795.8
308.15	10000.00	800.1
308.15	15000.00	803.8
308.15	20000.00	807.5
308.15	25000.00	811.1
308.15	30000.00	814.5
308.15	35000.00	817.8
308.15	40000.00	821.0
308.15	45000.00	824.1
308.15	50000.00	827.1
308.15	55000.00	830.0
308.15	60000.00	832.7
318.15	100.00	783.4
318.15	1000.00	784.2
318.15	5000.00	787.9
318.15	10000.00	792.2
318.15	15000.00	796.3
318.15	20000.00	800.2
318.15	25000.00	803.9
318.15	30000.00	807.5
318.15	35000.00	810.9
318.15	40000.00	814.2
318.15	45000.00	817.5
318.15	50000.00	820.5
318.15	55000.00	823.6
318.15	60000.00	825.8
328.15	100.00	775.0
328.15	1000.00	775.9
328.15	5000.00	779.7
328.15	10000.00	784.2
328.15	15000.00	788.5
328.15	20000.00	792.6
328.15	25000.00	796.5
328.15	30000.00	800.2
328.15	35000.00	803.8
328.15	40000.00	807.2
328.15	45000.00	810.6
328.15	50000.00	813.8
328.15	55000.00	816.9
328.15	60000.00	819.8
338.15	100.00	766.3
338.15	1000.00	767.2
338.15	5000.00	771.3
338.15	10000.00	776.1
338.15	15000.00	780.6
338.15	20000.00	784.9
338.15	25000.00	789.0
338.15	30000.00	792.9
338.15	35000.00	796.6
338.15	40000.00	800.2
338.15	45000.00	803.7
338.15	50000.00	807.0
338.15	55000.00	810.3
338.15	60000.00	813.4
348.15	100.00	757.2
348.15	1000.00	758.3
348.15	5000.00	762.6
348.15	10000.00	767.7
348.15	15000.00	772.5
348.15	20000.00	777.0
348.15	25000.00	781.3
348.15	30000.00	785.4
348.15	35000.00	789.3
348.15	40000.00	793.0
348.15	45000.00	796.6
348.15	50000.00	800.1
348.15	55000.00	803.5
348.15	60000.00	806.5
358.15	100.00	747.7
358.15	1000.00	748.8
358.15	5000.00	753.5
358.15	10000.00	758.8
358.15	15000.00	764.0
358.15	20000.00	768.7
358.15	25000.00	773.3
358.15	30000.00	777.5
358.15	35000.00	781.6
358.15	40000.00	785.5
358.15	45000.00	789.3
358.15	50000.00	792.9
358.15	55000.00	796.4
358.15	60000.00	799.6
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
303.20	1000.00	796.7
303.20	2000.00	797.5
303.20	3000.00	798.3
303.20	4000.00	799.2
303.20	5000.00	799.9
303.20	6000.00	800.7
303.20	7000.00	801.5
303.20	8000.00	802.3
303.20	9000.00	803.1
303.20	10000.00	803.9
323.20	1000.00	779.0
323.20	2000.00	779.9
323.20	3000.00	780.8
323.20	4000.00	781.7
323.20	5000.00	782.6
323.20	6000.00	783.5
323.20	7000.00	784.4
323.20	8000.00	785.3
323.20	9000.00	786.2
323.20	10000.00	787.0
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.15	100.00	803.85
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	799.66
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
288.15	100.00	807.62
288.15	5000.00	811.32
288.15	10000.00	814.7
288.15	15000.00	817.95
288.15	20000.00	821.27
288.15	25000.00	824.24
288.15	30000.00	827.24
288.15	35000.00	830.04
288.15	40000.00	832.73
293.15	100.00	803.57
293.15	5000.00	807.24
293.15	10000.00	810.8
293.15	15000.00	814.22
293.15	20000.00	817.46
293.15	25000.00	820.74
293.15	30000.00	823.7
293.15	35000.00	826.5
293.15	40000.00	829.09
298.15	100.00	799.61
298.15	5000.00	803.49
298.15	10000.00	807.15
298.15	15000.00	810.5
298.15	20000.00	813.78
298.15	25000.00	816.92
298.15	30000.00	820.04
298.15	35000.00	822.87
298.15	40000.00	825.81
303.15	100.00	795.62
303.15	5000.00	799.57
303.15	10000.00	803.13
303.15	15000.00	806.69
303.15	20000.00	810.14
303.15	25000.00	813.48
303.15	30000.00	816.64
303.15	35000.00	819.75
303.15	40000.00	822.6
308.15	100.00	791.31
308.15	5000.00	795.4
308.15	10000.00	799.21
308.15	15000.00	802.79
308.15	20000.00	806.37
308.15	25000.00	809.72
308.15	30000.00	813.03
308.15	35000.00	816.12
308.15	40000.00	819.06
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	81.50	799.54
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.15	100.00	803.17
293.15	5000.00	807.25
293.15	10000.00	811.02
293.15	15000.00	814.54
293.15	20000.00	817.87
293.15	25000.00	821.05
293.15	30000.00	824.15
293.15	35000.00	827.21
303.15	100.00	795.52
303.15	5000.00	799.83
303.15	10000.00	803.8
303.15	15000.00	807.49
303.15	20000.00	810.95
303.15	25000.00	814.23
303.15	30000.00	817.38
303.15	35000.00	820.48
313.15	100.00	787.3
313.15	5000.00	791.61
313.15	10000.00	795.67
313.15	15000.00	799.52
313.15	20000.00	803.19
313.15	25000.00	806.72
313.15	30000.00	810.15
313.15	35000.00	813.5
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
303.15	100.00	795.6
303.15	5000.00	799.5
303.15	10000.00	803.4
303.15	15000.00	807.0
303.15	20000.00	810.5
303.15	25000.00	813.9
303.15	30000.00	817.2
313.15	100.00	787.6
313.15	5000.00	791.6
313.15	10000.00	795.7
313.15	15000.00	799.5
313.15	20000.00	803.2
313.15	25000.00	806.7
313.15	30000.00	810.1
323.15	100.00	779.1
323.15	5000.00	783.4
323.15	10000.00	787.7
323.15	15000.00	791.7
323.15	20000.00	795.6
323.15	25000.00	799.3
323.15	30000.00	802.9
333.15	100.00	770.6
333.15	5000.00	775.1
333.15	10000.00	779.6
333.15	15000.00	783.9
333.15	20000.00	787.9
333.15	25000.00	791.8
333.15	30000.00	795.5
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.15	100.00	810.9
283.15	5000.00	814.7
283.15	10000.00	818.1
283.15	15000.00	821.7
283.15	20000.00	824.9
298.15	100.00	799.0
298.15	5000.00	803.0
298.15	10000.00	806.9
298.15	15000.00	810.6
298.15	20000.00	814.1
313.15	100.00	786.8
313.15	5000.00	791.2
313.15	10000.00	795.3
313.15	15000.00	799.3
313.15	20000.00	803.1
328.15	100.00	774.5
328.15	5000.00	779.1
328.15	10000.00	783.7
328.15	15000.00	787.8
328.15	20000.00	791.9
Reference

Speed of sound, m/s

Operational condition: Frequency, MHz = 8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Speed of sound, m/s - Liquid
253.15	102.00	1368.034
253.15	5133.00	1393.016
253.15	10109.00	1416.633
253.15	15198.00	1439.865
253.15	20092.00	1461.442
253.15	25341.00	1483.73
253.15	30423.00	1504.606
273.15	101.00	1293.525
273.15	5181.00	1320.802
273.15	10163.00	1346.251
273.15	15287.00	1371.412
273.15	20261.00	1394.803
273.15	25076.00	1416.612
273.15	30164.00	1438.924
293.15	105.00	1222.539
293.15	5042.00	1251.176
293.15	10141.00	1279.332
293.15	15272.00	1306.262
293.15	20136.00	1330.72
293.15	25068.00	1354.567
293.15	30231.00	1378.484
313.15	108.00	1154.108
313.15	5139.00	1185.752
313.15	10136.00	1215.403
313.15	15128.00	1243.591
313.15	20151.00	1270.557
313.15	25136.00	1296.129
313.01	30237.00	1321.177
333.15	101.00	1086.768
333.15	5018.00	1120.458
333.15	10050.00	1152.816
333.15	15186.00	1183.885
333.15	20183.00	1212.543
333.15	25121.00	1239.487
333.15	30028.00	1265.042
353.15	104.00	1018.903
353.15	5034.00	1055.962
353.15	10009.00	1090.768
353.15	15132.00	1124.22
353.15	20099.00	1154.783
353.15	25054.00	1183.626
353.15	30493.00	1213.605
Reference

Operational condition: Frequency, MHz = 8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Speed of sound, m/s - Liquid
249.99	100.00	1382.6
218.20	102.00	1512.0
299.97	138.00	1199.6
249.99	177.00	1383.0
350.05	270.00	1030.8
400.05	307.00	847.6
218.26	875.00	1515.2
400.05	947.00	854.9
350.07	997.00	1036.3
450.12	1081.00	636.4
249.99	1128.00	1387.7
299.96	1174.00	1206.0
350.07	2073.00	1044.4
218.21	2111.00	1520.8
400.05	2155.00	867.0
450.12	2181.00	653.9
250.01	2296.00	1393.4
299.96	2560.00	1214.3
500.31	4798.00	438.4
400.03	4879.00	893.3
218.26	5018.00	1533.1
299.98	5042.00	1228.8
450.11	5172.00	697.0
350.07	5244.00	1067.5
249.97	5362.00	1408.3
249.94	9322.00	1427.1
218.32	9465.00	1551.0
299.98	9515.00	1254.1
500.32	9558.00	542.3
350.06	9697.00	1098.3
400.07	9768.00	936.6
450.11	9782.00	754.2
218.35	19810.00	1591.6
299.96	19849.00	1308.7
500.32	19968.00	690.2
400.07	19974.00	1015.3
350.08	20259.00	1164.3
450.10	20385.00	860.0
249.90	20903.00	1478.7
400.06	27823.00	1068.3
218.34	29071.00	1626.6
450.11	30113.00	938.6
399.98	30784.00	1087.2
500.31	30851.00	799.1
299.96	39521.00	1400.6
249.93	39564.00	1553.9
500.28	39800.00	870.0
450.13	40189.00	1008.7
399.96	40232.00	1142.9
350.04	40537.00	1273.0
218.31	49499.00	1698.1
299.96	49960.00	1444.6
450.13	50091.00	1069.5
399.98	50284.00	1196.8
500.30	50346.00	946.6
350.03	52186.00	1327.6
249.94	59448.00	1625.8
399.97	59616.00	1242.9
500.31	60509.00	1009.7
350.04	60588.00	1364.3
218.32	61345.00	1736.4
500.31	77533.00	1102.4
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Speed of sound, m/s - Liquid
100.00	293.19	1222.98
100.00	298.12	1205.93
100.00	303.12	1188.72
100.00	308.20	1171.37
100.00	313.17	1154.51
100.00	318.20	1137.48
15200.00	293.12	1308.47
15200.00	298.11	1292.86
15200.00	303.14	1277.31
15200.00	308.20	1263.59
15200.00	313.16	1248.7
30400.00	293.22	1379.93
30400.00	298.15	1365.6
30400.00	303.24	1350.89
30400.00	308.13	1336.85
30400.00	313.16	1322.58
30400.00	318.16	1308.73
45590.00	293.21	1444.18
45590.00	298.14	1430.65
45590.00	303.13	1417.04
45590.00	308.13	1403.65
45590.00	313.16	1390.41
45590.00	318.14	1377.4
60790.00	293.21	1502.84
60790.00	298.14	1490.03
60790.00	303.20	1477.02
60790.00	308.13	1464.46
60790.00	313.17	1451.85
60790.00	318.12	1439.64
75990.00	293.20	1557.22
75990.00	298.14	1544.87
75990.00	303.15	1532.53
75990.00	308.12	1520.4
75990.00	313.16	1508.49
75990.00	318.12	1496.85
91190.00	293.20	1607.57
91190.00	298.14	1595.85
91190.00	303.17	1584.03
91190.00	308.20	1572.36
91190.00	313.15	1561.08
91190.00	318.12	1549.89
101320.00	293.18	1639.47
101320.00	298.14	1628.0
101320.00	303.17	1616.49
101320.00	308.19	1605.09
101320.00	313.15	1594.14
101320.00	318.11	1583.33
111450.00	293.17	1669.92
111450.00	298.14	1658.78
111450.00	303.19	1647.55
111450.00	308.16	1636.69
111450.00	313.22	1625.76
111450.00	318.17	1615.27
121580.00	293.16	1699.12
121580.00	298.14	1688.24
121580.00	303.18	1677.36
121580.00	308.11	1666.98
121580.00	313.17	1656.22
121580.00	318.17	1645.95
Reference

Molar volume, m3/mol

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Molar volume, m3/mol - Liquid
298.15	100.00	0.0001
298.15	10000.00	0.0001
313.15	100.00	0.0001
313.15	10000.00	0.0001
328.15	100.00	0.0001
328.15	10000.00	0.0001
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 5193.51]	kPa	[284.20; 536.78]	The Yaw...
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.58913e+01
Coefficient B			-3.49716e+03
Coefficient C			-6.00740e+01
Temperature range, min.			284.20
Temperature range, max.			536.78
Pvap	1.33	kPa	284.20	Calculated Property
Pvap	7.57	kPa	312.26	Calculated Property
Pvap	30.35	kPa	340.33	Calculated Property
Pvap	94.50	kPa	368.39	Calculated Property
Pvap	243.45	kPa	396.46	Calculated Property
Pvap	542.12	kPa	424.52	Calculated Property
Pvap	1076.63	kPa	452.59	Calculated Property
Pvap	1951.03	kPa	480.65	Calculated Property
Pvap	3282.18	kPa	508.72	Calculated Property
Pvap	5193.51	kPa	536.78	Calculated Property
Pvap	[6.41e-10; 4954.75]	kPa	[146.95; 536.71]	KDB Vap...
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			7.17170e+01
Coefficient B			-8.00269e+03
Coefficient C			-7.70223e+00
Coefficient D			3.95045e-07
Temperature range, min.			146.95
Temperature range, max.			536.71
Pvap	6.41e-10	kPa	146.95	Calculated Property
Pvap	2.13e-05	kPa	190.26	Calculated Property
Pvap	0.01	kPa	233.56	Calculated Property
Pvap	0.62	kPa	276.87	Calculated Property
Pvap	10.27	kPa	320.18	Calculated Property
Pvap	76.88	kPa	363.48	Calculated Property
Pvap	341.14	kPa	406.79	Calculated Property
Pvap	1054.26	kPa	450.10	Calculated Property
Pvap	2514.29	kPa	493.40	Calculated Property
Pvap	4954.75	kPa	536.71	Calculated Property

Similar Compounds

Find more compounds similar to 1-Propanol.

Mixtures

• 1-Propanol + Isopropyl Alcohol
• Aniline + 1-Propanol
• 1-Propanol + Acetonitrile
• Benzene + 1-Propanol
• 1-Propanol + Toluene
• Benzene + 1-Propanol + 2-Pyrrolidinone
• 1-Propanol + Toluene + 2-Pyrrolidinone
• 1-Propanol + Acetic acid, methyl ester
• Benzene + 1-Propanol + Cyclohexane
• 1-Propanol + 1-Propanamine, N-propyl-
• 1-Propanol + Piperazine, 1-methyl-
• 1-Propanol + Tetrahydrofuran
• 1-Propanol + Diisopropyl ether
• Benzene + 1-Propanol + Diisopropyl ether
• 1,3-Dioxolane + 1-Propanol + Water
• 1-Propanol + Phenol, 2-methyl-
• 1-Propanol + p-Cresol
• 1-Propanol + 2-Butanone + Benzene, 1,3-dichloro-
• 1-Propanol + Di-n-propyl ether
• 1-Propanol + 1-Pentanol

Find more mixtures with 1-Propanol.

Sources

• KDB Pure (Korean Thermophysical Properties Databank)
• KDB Vapor Pressure Data
• Crippen Method
• Speeds of Sound and Isentropic Compressibilities in Binary Mixtures of 2-Propanol with Several 1-Alkanols at 298.15K
• Densities and Volumetric Properties of Binary Mixtures of Aniline with 1-Propanol, 2-Propanol, 2-Methyl-1-Propanol, and 2-Methyl-2-Propanol at Temperatures from 293.15 to 318.15 K
• Application of the Extended Langmuir Model for the Determination of Lyophobicity of 1-Propanol in Acetonitrile
• Topological Investigations of Excess Molar Volumes and Excess Isentropic Compressibilities of Ternary Mixtures Containing Pyrrolidin-2-one at 308.15 K
• Experimental Determination of Densities and Isobaric Vapor Liquid Equilibria of Methyl Acetate and Ethyl Acetate with Alcohols (C3 and C4) at 0.3 MPa
• Solubility of Baicalein in Different Solvents from (287 to 323) K
• Fluid Phase Topology of Benzene + Cyclohexane + 1-Propanol at 101.3 kPa
• Isobaric vapor-liquid equilibria for 1-propanol +water + copper(II) chloride at 100 kPa
• Solubility of thiopene in carbon dioxide and carbon dioxide + 1-propanol mixtures at temperatures from 313 to 363K
• Thermodynamics of mixtures with strongly negative deviations from Raoult s law Part 9. Vapor liquid equilibria for the system 1-propanol + di-n-propylamine at six temperatures between 293.15 and 318.15K
• Determination of activity coefficients at infinite dilution of organic solutes in the ionic liquid, trihexyl(tetradecyl)-phosphonium tris(pentafluoroethyl) trifluorophosphate, by gas liquid chromatography
• Viscosities and densities for binary mixtures of N-methylpiperazine with methanol, ethanol, n-propanol, iso-propanol, n-butanol and iso-butanol at 293.15, 298.15 and 303.15K
• Prediction and experimental verification of the effect of salt on the vapour liquid equilibrium of ethanol/1-propanol/water mixture
• Thermodynamic properties of mixtures containing ionic liquids Vapor pressures and activity coefficients of n-alcohols and benzene in binary mixtures with 1-methyl-3-butyl-imidazolium bis(trifluoromethyl-sulfonyl) imide
• Ultrasonic velocity, viscosity and excess properties of binary mixture of tetrahydrofuran with 1-propanol and 2-propanol
• Salt effect on vapor liquid equilibria for binary systems of propanol/CaCl2 and butanol/CaCl2
• Measurement of infinite dilution activity coefficients of 1-alkanols (C1 C5) in water as a function of temperature (273 373 K)
• Total pressure and excess Gibbs energy for the ternary mixture di-isopropyl ether + 1-propanol + benzene and its corresponding binary systems at 313.15K
• (Liquid + liquid) equilibria of (water + 1-propanol + solvent) at T = 298.2K
• Effect of anion fluorination in 1-ethyl-3-methylimidazolium as solvent for the liquid extraction of ethanol from ethyl tert-butyl ether
• Viscous synergy and antagonism and isentropic compressibility of ternary mixtures containing 1,3-dioxolane, water and monoalkanols at 303.15K
• Activity coefficients of the binary mixtures of a-cresol or p-cresol with C l-C4 aliphatic alcohols near ambient pressure
• Excess molar volumes of ternary mixtures of 1,3-dichlorobenzene and methyl ethyl ketone with 1-alkanols at 303.15K
• Volumetric and derivative properties under pressure for the system 1-propanol + toluene: A discussion of PC-SAFT and SAFT-VR
• Isobaric vapor-liquid equilibria for the binary systems 1-propyl alcohol + dipropyl ether and 1-butyl alcohol + dibutyl ether at 20 and 101.3 kPa
• Vapor liquid equilibria in the ternary system dipropyl ether + 1-propanol + 1-pentanol and the binary systems dipropyl ether + 1-pentanol, 1-propanol + 1-pentanol at 101.3 kPa
• Vapor liquid equilibria for the ternary mixture of carbon dioxide + 1-propanol + propyl acetate at elevated pressures
• Phase equilibria of water + 1-propanol + solvent (n-amyl acetate, cyclohexanol, and cyclohexyl acetate) at T = 298.2K
• Phase equilibria involved in extractive distillation of dipropyl ether + 1-propyl alcohol using 2-ethoxyethanol as entrainer
• Vapor liquid equilibrium, densities, and interfacial tensions for the system ethyl 1,1-dimethylethyl ether (ETBE) + propan-1-ol
• High-pressure vapor liquid equilibria for CO2 + alkanol systems and densities of n-dodecane and n-tridecane
• Volumetric properties of the boldine + alcohol mixtures at atmospheric pressure from 283.15 to 333.15K A new method for the determination of the density of pure boldine
• Liquid liquid equilibria for the ternary systems water + 1-propanol + methyl methacrylate, +butyl methacrylate, and +isobutyl methacrylate
• Measurement of vapor.liquid equilibria (VLE) and excess enthalpies (HE) of binary systems with 1-alkyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide and prediction of these properties and A using modified UNIFAC (Dortmund)
• Determination of partial molar excess enthalpies at infinite dilution for the systems four alcohols + [bmim]PF6 at different temperatures by isothermal titration calorimeter
• Isothermal vapor liquid equilibrium at 303.15K and excess molar volumes at 298.15 K for the ternary system of propyl vinyl ether + 1-propanol + 2,2,4-trimethyl-pentane and its binary sub-systems
• Solubilities of rutin in eight solvents at T = 283.15, 298.15, 313.15, 323.15, and 333.15K
• Excess molar enthalpy of 1-alkanol + 1-octene mixtures at 298.15K Experimental results and theoretical description by means of the ERAS and TB models
• Apparent molar volume, isentropic compressibility and conductivity of di-sodium hydrogen phosphate in water and in aqueous solutions of 1-propanol
• Liquid liquid equilibria of the systems dipropyl ether + n-propanol +water and dipropyl ether + n-propanol + ethylene glycol at different temperatures
• Limiting activity coefficients in binary mixtures of 1-alkanols and ethylbenzene
• Influence of chain length and degree of branching of alcohol + chlorobenzene mixtures on determination and modelling of VE by CEOS and CEOS/GE mixing rules
• Volumetric, isentropic compressibility and electrical conductivity of solutions of tri-sodium phosphate in 1-propanol +water mixed-solvent media over the temperature range of 283.15 303.15K
• Thermodynamic properties of mixtures containing alkoxypropanol and n-alkanol
• Vapour liquid equilibria, azeotropic data, excess enthalpies, activity coefficients at infinite dilution and solid liquid equilibria for binary alcohol ketone systems
• Experimental densities and derived thermodynamic properties of liquid propan-1-ol at temperatures from 298 to 423K and at pressures up to 40MPa
• Excess molar enthalpies of ethyl acetoacetate + (methanol, +ethanol, +1-propanol, and +2-propanol) at T = (298.15, 313.15 and 328.15)K and p = (0.1 and 10.0)MPa
• Liquid liquid equilibria for the binary system of di-isopropyl ether (DIPE) +water in between 288.15 and 323.15K and the ternary systems of DIPE +water + C1 C4 alcohols at 298.15K
• A new high-pressure vapour liquid equilibrium apparatus
• Solubility of l-serine, l-threonine and l-isoleucine in aqueous aliphatic alcohol solutions
• Isobaric vapour liquid equilibria for binary systems of 2-butanone with ethanol, 1-propanol, and 2-propanol at 20 and 101.3 kPa
• Study of the effect of increasing the chain length of the alkane in excess molar enthalpies of mixtures containing methyl tert-butyl ether, 1-propanol, alkane
• Isothermal vapor liquid equilibrium at 333.15K and excess molar volumes at 298.15K for the ternary system di-isopropyl ether + n-propyl alcohol + toluene and its binary subsystems
• Isothermal vapor liquid equilibrium at 323.15K and excess molar volumes and refractive indices at 298.15K for the ternary system propyl vinyl ether + 1-propanol + benzene and its binary sub-systems
• Measurement and correlation of vapor pressure of benzene and thiophene with BMIM][PF6] and [BMIM][BF4] ionic liquids
• Solubility of antioxidant 1010 in pure alkanols
• Measurement and prediction of tie-line data for mixtures of (water + 1-propanol + diisopropyl ether): LLE diagrams as a function of temperature
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium trifluoromethanesulfonate using GLC
• Solubility and limiting activity coefficient of simvastatin in different organic solvents
• Phase equilibria of glycerol containing systems and their description with the Cubic-Plus-Association (CPA) Equation of State
• 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
• Measurement and prediction of multicomponent diffusion coefficients in four ternary liquid systems
• Solubility of CF4 in lower alcohols
• Liquid-liquid equilibrium of (water + 1-propanol + 1-pentanol) system at 298.15 and 323.15 K
• New analytic apparatus for experimental determination of vapor-liquid equilibria and saturation densities
• Isothermal vapour liquid equilibria in the binary and ternary systems consisting of an ionic liquid, 1-propanol and CO2
• Isobaric vapor-liquid equilibria for water + n-propanol + n-butanol ternary system at atmospheric pressure
• Solubilities of cefodizime disodium in aqueous alcohol mixtures at atmospheric pressure and different temperatures
• 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
• Solubility of alpha-form and beta-form of L-glutamic acid in different aqueous solvent mixtures
• Phase equilibria on binary systems containing diethyl sulfide
• Solubility of HFCs in lower alcohols
• VLE of CO2 + glycerol + (ethanol or 1-propanol or 1-butanol)
• Experimental measurement and modeling of solubility of LiBr and LiNO3 in methanol, ethanol, 1-propanol, 2-propanol and 1-butanol
• Vapor-liquid equilibria of ternary systems with 1-ethyl-3-methylimidazolium ethyl sulfate using headspace gas chromatography
• P-x data for binary systems using a novel static total pressure apparatus
• Solubility of itaconic acid in different organic solvents: Experimental measurement and thermodynamic modeling
• Determination of the crystallization thermodynamics and kinetics of L-tryptophan in alcohols - water system
• Study of the influence of the structure of the alcohol on vapor pressures and osmotic coefficients of binary mixtures alcohol + 1-hexyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide at T = 323.15 K
• Study of the liquid-liquid equilibrium of 1-propanol + manganese sulphate and 2-propanol + lithium sulphate aqueous two-phase systems at different temperatures: Experiment and correlation
• Solubility of caprolactam in different organic solvents
• Determination of the solubility, dissolution enthalpy and entropy of pyrene in different solvents
• Thermodynamics of the solubility of lomefloxacin in methanol, ethanol, 1-propanol, 2-propanol, acetone, and chloroform from 293.15 to 323.15 K
• Thermodynamic study of aqueous two phase systems for some aliphatic alcohols + sodium thiosulfate + water
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid ethyl(2-hydroxyethyl)dimethyl-ammonium diethylphosphate using gas liquid chromatography
• Solid-liquid phase equilibrium of glyphosate in selected solvents
• Activity coefficients at infinite dilution of organic solutes in 1-octyl-3-methylimidazolium nitrate using gas-liquid chromatography
• Liquid liquid equilibrium of 1-propanol, 2-propanol, 2-methyl-2-propanol or 2-butanol + sodium sulfite + water aqueous two phase systems
• Vapour-liquid and chemical equilibria in the ethyl ethanoate + ethanol + propyl ethanoate + propanol system accompanied with transesterification reaction
• Solubility of triclosan and iodopropynyl butylcarbamate in pure alkanols at several temperatures
• Measurement and correlation for solubility of levofloxacin in six solvents at temperatures from 288.15 to 328.15 K
• Solubility of lansoprazole in different solvents
• Determination of the solubility, dissolution enthalpy and entropy of suberic acid in different solvents
• Isobaric VLE at 0.6 MPa for binary systems isobutyl acetate + ethanol, + 1-propanol or + 2-propanol
• Excess molar volumes, excess molar enthalpies and refractive index deviations for binary mixtures of propan-1-ol, butan-1-ol and pentan-1-ol with 2,2,4-trimethylpentane at 298.15 K
• The study of phase behavior of aqueous 1-propanol/2-propanol/2-butanol/2-methyl-2-propanol systems in the presence of disodium tartrate or disodium succinate at T = 298.15 K
• Solid liquid equilibrium of 1-hydroxyethane-1,1-diphosphonic acid in different solvents
• Prediction of different thermodynamic properties for systems of alcohols and sulfate-based anion Ionic Liquids using modified UNIFAC
• Solubility of dimethyl fumarate in water + (methanol, ethanol, 1-propanol) from (278.15 to 333.15) K
• Correlation of solubility of pioglitazone hydrochloride in different binary solvents
• Solubility of citric acid in water, ethanol, n-propanol and in mixtures of ethanol + water
• The effect of temperature on the liquid-liquid equilibria of somealiphatic alcohols + di-sodium hydrogen citrate + water systems: Experimental and correlation
• Using binary mixtures of dicationic ionic liquids for determination ofactivity coefficients at infinite dilution by gas-liquid chromatography
• Thermodynamic and spectral investigations of binary liquid mixturesof 2-butoxy ethanol with alcohols at temperature range of 293.15-313.15 K
• Measurement and correlation solubility and mixing properties of dimethyl succinylsuccinate in pure and mixture organic solvents from (278.15 to 333.15) K
• Biobutanol and n-propanol recovery using a low density phosphonium based ionic liquid at T = 298.15 K and p = 1 atm
• A novel dynamic recirculating apparatus for vapour-liquid equilibrium measurements at moderate pressures and temperatures
• Measurement and correlation solubility and mixing properties of L-malic acid in pure and mixture organic solvents
• Phase equilibria and excess molar enthalpies study of the binary systems (pyrrole + hydrocarbon, or an alcohol) and modeling
• Liquid liquid equilibria of 4-methyl-2-pentanone + 1-propanol or 2-propanol + water ternary systems: Measurements and correlation at different temperatures
• (p, VE, T) Measurements of mixtures (DBE + alcohol) at temperaturesfrom (293.15 to 353.15) K and at pressures up to 140 MPa
• Liquid-liquid equilibria of 1-octyl-3-methylimidazolium hexafluorophosphate with 1-propanol or tert-butanol in the critical region
• Thermodynamics of fenofibrate and solubility in pure organic solvents
• Present status of the modified UNIFAC Model for the prediction of phase equilibria and excess enthalpies for systems with ionic liquids
• Thermodynamics of risperidone and solubility in pure organic solvents
• Solubility, liquid-liquid equilibrium and critical states for the system acetic acid + n-propanol + n-propyl acetate + water at 293.15 K and 303.15 K
• Measurement and modeling of volumetric properties and speeds of sound of several mixtures of alcohol liquids containing 1-propanol and 2-propanol at T= (298.15 - 323.15) K and ambient pressure
• Micellization properties and related thermodynamic parameters ofaqueous sodium dodecyl sulfate and sodium dodecyl sulfonatesolutions in the presence of 1-propanol
• Experimental and theoretical study of interaction between organic compounds and 1- (4-sulfobutyl)-3-methylimidazolium based ionic liquids
• Solubility of N-Ethylcarbazole in different organic solvent at 279.15 - 319.15 K
• Excess molar enthalpies for binary mixtures of n-propanol, acetic acid, and n-propyl acetate at 313.15 K and atmospheric pressure
• Solid-liquid equilibrium of sulbactam in pure solvents and binary solvent mixtures
• Experimental study of the density and derived partial molar volumes of complex ternary water+1-propanol+Li2SO4 mixtures at temperatures from (303 to 448) K and pressures up to 40 MPa
• Measurement, correlation, and prediction of vapor pressure for binary and ternary systems containing an ionic liquid 1,3-dimethylimidazolium methylsulfate
• Study of interaction between organic compounds and mono or dicationic oxygenated ionic liquids using gas chromatography
• Isobaric vapor liquid equilibrium for the binary systems of 1-propanol + 1-(methoxymethoxy)-butane and 1-butanol + 1-(methoxymethoxy)- butane at 101.3 kPa
• Solubilities of phosphoric acid, P,P0-1,4-phenylene P,P,P0,P0-tetraphenyl ester in the organic solvents
• Correlation of solubility and calculation of thermodynamic properties of guanidine nitrate in different solvents
• Solubility of methylphosphonic acid in selected organic solvents
• Determination and correlation of solubility and solution thermodynamics of coumarin in different pure solvents
• Separation of pyridine from heptane with tricyanomethanide-based ionic liquids
• Solid-liquid equilibrium of diphenyl anilinophosphonate in the different organic solvents
• Measurement, correlation, and prediction of vapor pressure for binary and ternary systems containing an alkylsulfate-based ionic liquid
• Liquid-liquid equilibria for water + 1-propanol (or 1-butanol) + potassium chloride + ammonium chloride quaternary systems at 298.15 K
• High-temperature vapor-liquid equilibrium for ethanol-1-propanol mixtures and modeling with SAFT-VR
• Measurements and correlations of density and viscosity for short chain (C1-C3) n-alcohol - water mixtures in the temperature range from 350.7 K to 476.2 K at pressures up to 40 MPa
• Isobaric (vapor-liquid) equilibria for binary systems of methanol + 1-(methoxymethoxy)- propane and 1-propanol + 1-(methoxymethoxy)-propane at 101.33 kPa
• Excess molar enthalpies of the ternary mixture n-propanol + acetic acid + water at 313.15 K and atmospheric pressure
• Activity coefficients at infinite dilution for different alcohols and ketones in [EMpy][ESO4]: Experimental data and modeling with PC-SAFT
• The liquid-liquid phase separation and crystallization of vanillin in 1-propanol/water solution
• Limiting activity coefficient measurements in binary mixtures of dichloromethane and 1-alkanols (C1 - C4)
• 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
• Liquid-liquid equilibrium for the quaternary system propionic acid + n-propanol + n-propyl propionate + water at 293.15, 313.15 and 333.15 K
• Measurement and correlation of phase equilibria for ternary systems of water + (ethanol / 1-propanol) + 1-decyl-3-methylimidazolium bis(trifluoromethylsulfonyl) imide at 298.15 K
• Determination and correlation of solubility and solution thermodynamics of ethenzamide in different pure solvents
• Measurement and correlation of liquid-liquid equilibria at different temperatures of water + 1-propanol + 1-ethyl-3- methylimidazolium bis(trifluoromethylsulfonyl)imide or 1-hexyl-3- methylimidazolium bis(trifluoromethylsulfonyl)imide ternary systems
• Determination and correlation of solubility of linezolid form II in different pure and binary solvents
• Evaluation of the solvent structural effect upon the vapor-liquid equilibrium of [C4C1im][Cl] + Alcohols
• Application of 1-hexyl-3-methylimidazolium trifluoromethanesulfonate to the removal of alcohol from mixtures with heptane
• Determination and correlation of solubility of N-methyl-3,4,5- trinitropyrazole (MTNP) in ten pure solvents from 283.15 K to 323.15 K
• Heterogeneous azeotropic distillation for the separation of n-propanol + water mixture using n-propyl acetate as entrainer
• High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
• Measurement and correlation of density and viscosity of n-alcohol-water mixtures at temperatures up to 618 K and at pressures up to 40 MPa
• Thermodynamic equilibrium of hydrocortisone form I in different solvent systems
• Solubility and dissolution characteristics of capecitabine in pure lower alcohols and water with methanol mixture solvents at atmospheric pressure and different temperatures
• Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
• Solubility and mixing thermodynamic properties of (2,4,6-trimethylbenzoyl) diphenylphosphine oxide in pure and binary solvents
• Measurements of activity coefficient at infinite dilution for organic solutes in tetramethylammonium chloride + ethylene glycol deep eutectic solvent using gas-liquid chromatography
• SLLE and SLLVE of the water + NH4Cl + 1-propanol system at 101.3 kPa
• Measurement and correlation of aqueous biphasic systems composed of alcohol (1-propanol/ 2-propanol/tert-butanol) + (NH4)2SO4 + H2O at 298 K and a textile dye partition.
• Capability study of 1-butyl-3- methylimidazolium bis(trifluoromethylsulfonyl)imide and trihexyl(tetradecyl)phosphonium bis(2,4,4-trimethylpentyl)phosphinate as solvents in the separation of 1-propanol from water
• Molecular dynamic simulation, molecular interactions and structural properties of 1-butyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide + 1-butanol/1- propanol mixtures at (298.15-323.15) K and 0.1 M Pa
• Solubility evaluation and thermodynamic modeling of beta-lapachone in water and ten organic solvents at different temperatures
• Solubility of 1-methyl-4-nitropyrazole in seventeen pure solvents at temperatures from 283.15 K to 323.15 K
• A systematic study on volumetric and transport properties of binary systems 1-propanol + n-hexadecane, 1-butanol + n-hexadecane and 1-propanol + ethyl oleate at different temperatures: Experimental and modeling
• Tetramethylammonium chloride + glycerol deep eutectic solvent as separation agent for organic liquid mixtures: Assessment from experimental limiting activity coefficients
• Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-butyl-1-methylpyrrolidinium dicyanamide
• Solubility determination and correlation of cyromazine in sixteen pure solvents and mixing properties of solutions
• New ionic liquid [P4,4,4,4][NTf2] in bio-butanol extraction on investigation of limiting activity coefficients
• Solid-liquid equilibria for selected binary systems containing diphenyl carbonate
• Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
• Dissolution behavior and thermodynamic properties of lapatinib ditosylate in pure and mixed organic solvents from T = (283.15-323.15) K
• Measurement and modeling of infinite dilution activity coefficients of organic compounds in an equimolar ionic liquid mixture of [Bmim]Cl and [Bmim][Tf2N]
• Application of trihexyltetradecylphosphonium dicyanamide ionic liquid for various types of separations problems: Activity coefficients at infinite dilution measurements utilizing GLC method
• Measurement of the thermal conductivity of biofuel mixtures: Methyl caprate components of biodiesel and alcohols
• Henry's constants and infinite dilution activity coefficients of propane, propene, butane, isobutene, 1-butene, isobutane, trans-2-butene and 1,3-butadiene in 1-propanol at T=(260 to 340) K
• Temperature dependence of the volumetric properties of some alkoxypropanols + n-alkanol mixtures
• (Vapor + liquid) equilibria for the binary mixtures (1-propanol + dibromomethane, or + bromochloromethane, or + 1,2-dichloroethane or +1-bromo-2-chloroethane) at T = 313.15 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)
• Excess molar enthalpies of ethylformate and (1-propanol, 2-propanol, 1-butanol, 2-butanol, and 1-pentanol) at T = (298.15 and 308.15) K and p = (5 and 10) MPa
• Experimental and predicted volumetric and refractive index properties of ternary mixtures of iodoethane with toluene and alcohols at temperature 298.15 K and pressure 101 kPa
• Excess molar volumes and partial molar volumes for (propionitrile + an alkanol) at T = 298.15 K and p = 0.1 MPa
• Physico-chemical and excess properties of the binary mixtures of methylcyclohexane + ethanol, + propan-1-ol, + propan-2-ol, + butan-1-ol, + 2-methyl-1-propanol, or 3-methyl-1-butanol at T = (298.15, 303.15, and 308.15) K
• Henry's law constants and infinite dilution activity coefficients of cis-2-butene, dimethylether, chloroethane, and 1,1-difluoroethane in methanol, 1-propanol, 2-propanol, 1-butanol, 2-butanol, isobutanol, tert-butanol, 1-pentanol, 2-pentanol, 3-pentanol, 2-methyl-1-butanol, 3-methyl-1-butanol, and 2-methyl-2-butanol
• Bubble point temperatures of the binary mixtures of nitrobenzene with C1 C4 aliphatic alcohols at 94.95 kPa
• Thermodynamic properties of (tetradecane + benzene, + toluene, + chlorobenzene, + bromobenzene, + anisole) binary mixtures at T = (298.15, 303.15, and 308.15) K
• Volumetric properties of binary mixtures of ionic liquid 1-butyl-3-methylimidazolium octylsulfate with water or propanol in the temperature range of 278.15 K to 328.15 K
• Viscosity, density, and speed of sound of methylcyclopentane with primary and secondary alcohols at T = (293.15, 298.15, and 303.15) K
• (Vapor + liquid) equilibria of the binary mixtures of m-cresol with C1 C4 aliphatic alcohols at 95.5 kPa
• Densities, viscosities, and ultrasonic velocity studies of binary mixtures of trichloromethane with methanol, ethanol, propan-1-ol, and butan-1-ol at T=(298.15 and 308.15) K
• Thermodynamic interactions in binary mixtures of anisole with ethanol, propan-1-ol, propan-2-ol, butan-1-ol, pentan-1-ol, and 3-methylbutan-1-ol at T = (298.15, 303.15, and 308.15) K
• Densities and derived thermodynamic properties of (2-methoxyethanol + 1-propanol, or 2-propanol, or 1,2-propandiol) at temperatures from T = (293.15 to 343.15) K
• 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
• Densities and volumetric properties of (formamide + ethanol, or 1-propanol, or 1,2-ethanediol, or 1,2-propanediol) mixtures at temperatures between 293.15 K and 318.15 K
• Molar excess enthalpies of binary mixtures of [tributyl phosphate + {CH3(CH2)nOH (n = 0 to 3)}] at 298.15 K
• Excess molar volumes of binary mixtures of 1,3-dimethylimidazolidin-2-one with an alkan-1-ol at the temperatures 283.15 K, 298.15 K, and 313.15 K
• Phase equilibria of didecyldimethylammonium nitrate ionic liquid with water and organic solvents
• Densities and viscosities of binary mixtures of {dimethylsulfoxide + aliphatic lower alkanols (C1 C3)} at temperatures from T = 303.15 K to T = 323.15 K
• Measurement of activity coefficients at infinite dilution in 1-hexadecyl-3-methylimidazolium tetrafluoroborate ionic liquid
• Measurement and correlation of solubility of trans-resveratrol in 11 solvents at T = (278.2, 288.2, 298.2, 308.2, and 318.2) K
• Densities and volumetric properties of (N-(2-hydroxyethyl)morpholine + ethanol, + 1-propanol, + 2-propanol, + 1-butanol, and + 2-butanol) at (293.15, 298.15, 303.15, 313.15, and 323.15) K
• Isobaric (vapour + liquid + liquid) equilibrium data for (di-n-propyl ether + n-propyl alcohol + water) and (diisopropyl ether + isopropyl alcohol + water) systems at 100 kPa
• Measurements of activity coefficients at infinite dilution of aromatic and aliphatic hydrocarbons, alcohols, and water in the new ionic liquid [EMIM][SCN] using GLC
• Volumetric, acoustic, and viscometric studies of molecular interactions in binary mixtures of dipropylene glycol dimethyl ether with 1-alkanols at 298.15 K
• Densities, excess molar volumes, speeds of sound and isothermal compressibilities for {2-(2-hexyloxyethoxy)ethanol + n-alkanol} systems at temperatures between (288.15 and 308.15) K
• Thermodynamic properties of solutions of sodium di-hydrogen phosphate in (1-propanol + water) mixed-solvent media over the temperature range of (283.15 to 303.15) K
• Mixing thermodynamic properties of 1-butyl-4-methylpyridinium tetrafluoroborate [b4mpy][BF4] with water and with an alkan-1ol (methanol to pentanol)
• Excess molar volumes and isentropic compressibility of binary systems {trioctylmethylammonium bis(trifluoromethysulfonyl)imide + methanol or ethanol or 1-propanol} at different temperatures
• Activity coefficients at infinite dilution of hydrocarbons, alkylbenzenes, and alcohols in the paramagnetic ionic liquid 1-butyl-3-methyl-imidazolium tetrachloridoferrate(III) using gas liquid chromatography
• 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
• Osmotic coefficients of binary mixtures of 1-butyl-3-methylimidazolium methylsulfate and 1,3-dimethylimidazolium methylsulfate with alcohols at T = 323.15 K
• Phase equilibria study of the binary systems (N-butyl-4-methylpyridinium tosylate ionic liquid + an alcohol)
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 4-methyl-N-butyl-pyridinium bis(trifluoromethylsulfonyl)-imide
• Density and viscosity of 1-butyl-3-methylimidazolium nitrate with ethanol, 1-propanol, or 1-butanol at several temperatures
• Vapour pressures and osmotic coefficients of binary mixtures of 1-ethyl-3-methylimidazolium ethylsulfate and 1-ethyl-3-methylpyridinium ethylsulfate with alcohols at T = 323.15 K
• Molar excess enthalpies at T = 298.15 K for (1-alkanol + dibutylether) systems
• Activity coefficients at infinite dilution for solutes in the trioctylmethylammonium bis(trifluoromethylsulfonyl)imide ionic liquid using gas liquid chromatography
• Thermophysical properties of the binary mixtures (1,8-cineole + 1-alkanol) at T = (298.15 and 313.15) K and at atmospheric pressure
• Measurement and modeling of high-pressure (vapour + liquid) equilibria of (CO2 + alcohol) binary systems
• Vapour pressures, osmotic and activity coefficients for binary mixtures containing (1-ethylpyridinium ethylsulfate + several alcohols) at T = 323.15 K
• Gas liquid chromatography measurements of activity coefficients at infinite dilution of various organic solutes and water in tri-iso-butylmethylphosphonium tosylate ionic liquid
• Isobaric (vapour + liquid) equilibria for the (1-propanol + 1-butanol) binary mixture at (53.3 and 91.3) kPa
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate [EMIM][TCB] using gas liquid chromatography
• Ultrasonic speeds and isentropic compressibilities of {difurylmethane + (C1 C6) n-alkanol} binary mixtures at T = 298.15 K
• 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
• Cloud point measurements of 1-butyl-2,3-dimethylimidazolium tetrafluoroborate with alcohols
• Measurement and correlation of solubilities of apigenin and apigenin 7-O-rhamnosylglucoside in seven solvents at different temperatures
• Measurements of activity coefficients at infinite dilution of organic compounds and water in isoquinolinium-based ionic liquid [C8iQuin][NTf2] using GLC
• Thermophysical properties of {(+-)-linalool + propan-1-ol}: A first stage towards the development of a green process
• Application of the ERAS model to volumetric properties of binary mixtures of banana oil with primary and secondary alcohols (C1- C4) at different temperatures
• 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
• Apparent molar volumes and compressibilities of tetrabutyl-ammonium bromide in organic solvents
• Measurement and modeling of osmotic coefficients of binary mixtures (alcohol + 1,3-dimethylpyridinium methylsulfate) at T = 323.15 K
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
• Volumetric and viscometric properties of binary mixtures of {methyl tert-butyl ether (MTBE) + alcohol} at several temperatures and p = 0.1 MPa: Experimental results and application of the ERAS model
• Determination and modelling of osmotic coefficients and vapour pressures of binary systems 1- and 2-propanol with CnMimNTf2 ionic liquids (n = 2, 3, and 4) at T = 323.15 K
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(3-hydroxypropyl)pyridinium bis(trifluoromethylsulfonyl)-amide
• Application of the extended real associated solution (ERAS) theory to excess molar enthalpies of benzaldehyde + 1-alkanols (C1 to C5) at T = 298.15 K
• Phase equilibrium in systems with ionic liquids: An example for the downstream process of the Biphasic Acid Scavenging utilizing Ionic Liquids (BASIL) process. Part I: Experimental data
• Thermodynamics and activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tetracyanoborate
• Ebulliometric determination and prediction of (vapor + liquid) equilibria for binary and ternary mixtures containing alcohols (C1 C4) and dimethyl carbonate
• Solubility of sodium 4-nitrotoluene-2-sulfonate in (propanol + water) and (ethylene glycol + water) systems
• Effect of the temperature on the physical properties of pure 1-propyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide and characterization of its binary mixtures with alcohols
• Interactions of volatile organic compounds with the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
• PrhoT measurements and derived properties of liquid 1-alkanols
• The buffering-out effect and phase separation in aqueous solutions of EPPS buffer with 1-propanol, 2-propanol, or 2-methyl-2-propanol at T = 298.15 K
• Solubilities of some organic solutes in 1-ethyl-3-methylimidazolium acetate. Chromatographic measurements and predictions from COSMO-RS
• Excess properties of binary mixtures containing 1-hexyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide ionic liquid and polar organic compounds
• 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
• Chemical calibration of Isothermal Titration Calorimeters: An evaluation of the dilution of propan-1-ol into water as a test reaction using different calorimeters, concentrations, and temperatures
• Properties of pure 1-methylimidazolium acetate ionic liquid and its binary mixtures with alcohols
• 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
• Determination and correlation of the solubility for diosgenin in alcohols solvents
• Acoustic, volumetric and osmotic properties of binary mixtures containing the ionic liquid 1-butyl-3-methylimidazolim dicyanamide mixed with primary and secondary alcohols
• Surface thermodynamics of binary mixtures of aliphatic alcohols in heavy water
• Experimental study on the calorimetric data of cyclohexanol with alkanols (C1-C4) and correlation with Wilson, NRTL and UNIQUAC models at 300 K
• Densities and derived thermodynamic properties of binary alkanol + boldine mixtures in the compressed liquid region
• 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
• Phase equilibrium measurements and thermodynamic modeling of methane alcohol systems at ambient temperature
• 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
• Measurement and correlation of the solubility of 2,3,4,5-tetrabromothiophene in different solvents
• Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds: Saturated fatty acids
• Experimental determination and modeling of excess molar volumes, viscosities and refractive indices of the binary systems (pyridine + 1-propanol, + 1,2-propanediol, + 1,3-propanediol, and + glycerol). New UNIFAC-VISCO parameters determination
• Thermodynamic investigation of the ATPSs composed of some (aliphatic alcohol + sodium carbonate + water) ternary systems
• Measurement and correlation of solubility of Tetracycline hydrochloride in six organic solvents
• 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
• Henry s constants and activity coefficients of some organic solutes in 1-butyl,3-methylimidazolium hydrogen sulfate and in 1-methyl,3-trimethylsilylmethylimidazolium chloride
• Densities, speeds of sound, and refractive indices for binary mixtures of 1-butyl-3-methylimidazolium methyl sulphate ionic liquid with alcohols at T = (298.15, 303.15, 308.15, and 313.15) K
• Solubility of salicylic acid in pure alcohols at different temperatures
• 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
• Experimental measurements and predictions of density, viscosity, and carbon dioxide solubility in methanol, ethanol, and 1-propanol
• Properties of pure n-butylammonium nitrate ionic liquid and its binary mixtures of with alcohols at T = (293.15 to 313.15) K
• Volume effects for binary mixtures of propane-1,2-diol with methanol, propan-1-ol, hexan-1-ol, octan-1-ol, or nonan-1-ol at temperatures (293.15 to 318.15) K
• Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds Part II: C18 fatty acids
• High-temperature vapour liquid equilibrium for the (water + alcohol) systems and modelling with SAFT-VR: 2. Water-1-propanol
• 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
• Osmotic and apparent molar properties of binary mixtures alcohol + 1-butyl-3-methylimidazolium trifluoromethanesulfonate ionic liquid
• Separation of thiophene from heptane with ionic liquids
• 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
• Solubility and phase behavior of binary systems containing salts based on transitional metals
• Quantitative NMR spectroscopy of binary liquid mixtures (aldehyde + alcohol) Part I: Acetaldehyde + (methanol or ethanol or 1-propanol)
• Ternary (liquid + liquid) equilibria for (water + 1-propanol + dimethyl carbonate, or diethyl carbonate) systems at several temperatures
• Study of surface tension and surface properties of binary systems of DMSO with long chain alcohols at various temperatures
• 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
• Excess molar enthalpies of {diethyl oxalate + (methanol, + ethanol, + 1-propanol, and + 2-propanol)} at T = (288.2, 298.2, 313.2, and 328.2) K and p = 101.3 kPa
• Vapour pressures and osmotic coefficients of binary mixtures containing alcohol and pyrrolidinium-based ionic liquids
• 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
• Quantitative NMR spectroscopy of binary liquid mixtures (aldehyde + alcohol). Part II: (Propanal or butanal or heptanal) + (methanol or ethanol or 1-propanol)
• Experimental and theoretical excess molar enthalpies of ternary and binary mixtures containing 2-Methoxy-2-Methylpropane, 1-propanol, heptane
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tricyanomethanide
• Biocompatible choline based ionic salts: Solubility in short-chain alcohols
• (Vapour + liquid) equilibria in the ternary system (acetonitrile + n-propanol + ethylene glycol) and corresponding binary systems at 101.3 kPa
• FT-IR studies on excess thermodynamic properties of binary liquid mixtures o-chlorotoluene with 1-propanol, 1-butanol, 1-pentanol, 1-hexanol and 1-heptanol at different temperatures
• Physical properties of the pure 1-methyl-1-propylpyrrolidinium bis(trifluoromethylsulfonyl)imide ionic liquid and its binary mixtures with alcohols
• Thermodynamics and activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylmorpholinium tricyanomethanide
• Study of molecular interactions in the mixtures of some primary alcohols with equimolar mixture of 1-propanol and alkylbenzoates at T = 303.15 K
• The study of activity coefficients at infinite dilution for organic solutes and water in 1-butyl-4-methylpyridinium dicyanamide, [B4MPy][DCA] using GLC
• Thermodynamics of (ketone + amine) mixtures. Part XI. Excess molar enthalpies at T = 298.15 K for the (1-propanol + N,N,N-triethylamine + 2-butanone) system
• Separation of sulfur compounds from alkanes with 1-alkylcyanopyridinium-based ionic liquids
• Osmotic coefficients and apparent molar volumes of 1-hexyl-3-methylimidazolium trifluoromethanesulfonate ionic liquid in alcohols
• 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
• Experimental study of the density and derived volumetric (excess, apparent, and partial molar volumes) properties of aqueous 1-propanol mixtures at temperatures from 298K to 582K and pressures up to 40MPa
• Osmotic coefficients of alcoholic mixtures containing BMpyrDCA: Experimental determination and correlation
• Effect of the alkyl side chain of the 1-alkylpiperidinium-based ionic liquids on desulfurization of fuels
• Determination and correlation of the solubility of four Bronsted-acidic ionic liquids based on benzothiazolium cations in six alcohols
• Measurement and correlation of critical properties for binary mixtures and ternary mixtures containing gasoline additives
• Quantitative NMR spectroscopy of binary liquid mixtures (aldehyde + alcohol). Part III: (1-decanal or 3-phenylpropanal or 2-chlorobenzaldehyde) + (methanol or ethanol or 1-propanol)
• Effect of the temperature on the physical properties of the pure ionic liquid 1-ethyl-3-methylimidazolium methylsulfate and characterization of its binary mixtures with alcohols
• Measurement, correlation and dissolution thermodynamics of biological active chalcone in organic solvents at different temperatures
• Solubility of climbazole in various alcohols at different temperatures
• Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
• Extraction desulfurization process of fuels with ionic liquids
• Determination and correlation of solubility of spironolactone form II in pure solvents and binary solvent mixtures
• Molecular interactions in binary mixtures of 1-butoxy-2-propanol with alcohols at different temperatures: A thermophysical and spectroscopic approach
• Determination and correlation of solubility of tylosin tartrate in alcohol mixtures
• A combined experimental and computational investigation of excess molar enthalpies of (nitrobenzene + alkanol) mixtures
• 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
• Excess enthalpies of ternary mixtures of (oxygenated additives + aromatic hydrocarbon) mixtures in fuels and bio-fuels: (Dibutyl-ether + 1-propanol + benzene), or toluene, at T = (298.15 and 313.15) K
• Isothermal (vapor + liquid) equilibria for the binary mixtures of (propylene oxide + ethanol) and (propylene oxide + 1-propanol) at several temperatures
• (Liquid + liquid) equilibria for (water + 1-propanol or acetone + .beta.-citronellol) at different temperatures
• 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
• Thermodynamic models for determination of the solubility of (-)-shikimic acid in different pure solvents and in (H2O + ethanol) binary solvent mixtures
• Properties of pure 1,1,3,3-tetramethylguanidine imidazole ionic liquid and its binary mixtures with alcohols at T = (293.15 to 313.15) K
• Excess molar enthalpies of R-fenchone + propan-1-ol or +propan-2-ol. Modeling with COSMO-RS and UNIFAC
• Activity coefficients at infinite dilution for organic solutes and water in 1-ethyl-1-methylpyrrolidinium lactate
• 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
• Measurements and equation-of-state modelling of thermodynamic properties of binary mixtures of 1-butyl-1-methylpyrrolidinium tetracyanoborate ionic liquid with molecular compounds
• (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)
• Volumetric and compressibility behaviour of poly(propylene glycol) - Amino acid aqueous solutions at different temperatures
• Experimental determination and correlation of the solubility of 4-hydroxy-2,5-dimethyl-3(2H)-furanone (DMHF) in six different solvents
• Solubility and solution thermodynamics of thymol in six pure organic solvents
• Speed of sound measurements of liquid C1-C4 alkanols
• Solubility modelling and thermodynamic dissolution functions of phthalimide in ten organic solvents
• Measurement and correlation of solubility of thiourea in two solvent mixtures from T = (283.15 to 313.15) K
• Solubility and solution thermodynamics of ethyl 5-amino-4-cyano-3-(2-ethoxy-2-oxoethyl)-2-thiophenecarboxylate in nine organic solvents at evaluated temperatures
• Solubility of 3-chloro-N-phenylphthalimide in ten organic solvents from T = (288.15 to 323.15) K: Determination and modelling
• Physicochemical properties of binary mixtures of 1,1,3,3-tetramethylguanidine imidazolide ionic liquid with water and alcohols
• A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
• Thermodynamic models for determination of the solubility of 4-(4-aminophenyl)-3-morpholinone in different pure solvents and (1,4-dioxane + ethyl acetate) binary mixtures with temperatures from (278.15 to 333.15) K
• (Vapor + liquid) equilibria of alcohol + 1-methyl-1-propylpiperidinium triflate ionic liquid: VPO measurements and modeling
• Experimental measurement and correlation of the solubility of aloe-emodin in seven pure solvents
• Determination and thermodynamic modeling of solid-liquid phase equilibrium for 3,5-dichloroaniline in pure solvents and ternary 3,5-dichloroaniline + 1,3,5-trichlorobenzene + toluene system
• Solubility determination and thermodynamic dissolution functions of 1,3-diphenylguanidine in nine organic solvents at evaluated temperatures
• Measurement and calculation of solid liquid equilibrium for ternary systems of 3,4-dichloronitrobenzene + 2,3-dichloronitrobenzene + ethanol/n-propanol
• Solubility determination and thermodynamic modeling of 5-nitro-8- hydroxyquinoline in ten organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
• Solubility and solution thermodynamics of 2-methyl-6-nitroaniline in ten organic solvents at elevated temperatures
• (Liquid + liquid) equilibria of four alcohol-water systems containing 1,8-cineole at T = 298.15 K
• Volumetric and viscometric study with FT-IR analysis of binary systems with diethyl succinate and alcohols
• 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
• Determination and correlation of solubility of 4'-bromomethyl-2-cyanobiphenyl in acetone + (ethanol, n-propanol, n-butanol) mixtures
• Solubility determination and thermodynamic modeling of 2,4-dinitroaniline in nine organic solvents from T = (278.15 to 318.15) K and mixing properties of solutions
• Solubility determination and thermodynamic modelling of terephthaldialdehyde in ten organic solvents from T = (273.15 to 318.15) K and mixing properties of solutions
• 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
• 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 of cefoxitin acid in different solvent systems
• Experimental study on the calorimetric data of 2-butoxyethanol with aliphatic alcohols (C1-C4) and correlation with the Wilson, NRTL and UNIQUAC models at T = 298 K
• 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
• Solubility of N-phenylanthranilic acid in nine organic solvents from T = (283.15 to 318.15) K: Determination and modelling
• Thermodynamic functions of 1-methyl-4-(methylsulfonyl)benzene solubility in nine organic solvents from T = (278.15 to 318.15) K
• Thermodynamic and spectroscopic properties of binary mixtures of n-butylammonium butanoate ionic liquid with alcohols at T = (293.15-313.15) K
• Solubility of oxcarbazepine in eight solvents within the temperature range T = (288.15 308.15) K
• Thermodynamic modelling for solubility of 4-nitrobenzaldehyde in different solvents at temperature range from (273.15 to 313.15) K and mixing properties of solutions
• Determination and modelling of troxerutin solubility in eleven mono-solvents and (1,4-dioxane + 2-propanol) binary solvents at temperatures from 288.15 K to 323.15 K
• Fully automatized apparatus for determining speed of sound for liquids in the temperature and pressure interval (283.15-343.15) K and (0.1-95) MPa
• Solubility determination and thermodynamic modelling of 3-amino-1,2,4-triazole in ten organic solvents from T = 283.15 K to T = 318.15 K and mixing properties of solutions
• Solubility determination and thermodynamic modeling of paclobutrazol in nine organic solvents from T = (278.15 to 318.15) K and mixing properties of solutions
• A green process for recovery of 1-propanol/2-propanol from their aqueous solutions: Experimental and MD simulation studies
• 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
• Thermodynamic modelling for solubility of 5-chloro-1-methyl-4-nitroimidazole in eleven organic solvents from T = (283.15 to 318.15) K
• Measurement and correlation of solubility of ciclesonide in seven pure organic solvents
• Thermodynamic study of solubility for 2-amino-4-chloro-6-methoxypyrimidine in twelve organic solvents at temperatures from 273.15 K to 323.15 K
• PVTx measurements and other derived volumetric properties of the binary ((1-propanol + n-pentane)) mixtures in the critical and supercritical regions
• Solid-liquid phase equilibrium and dissolution properties of ethyl vanillin in pure solvents
• 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
• Determination and thermodynamic modelling for 2-methyl-6-nitroaniline solubility in binary solvent mixtures of ethyl acetate + (methanol, ethanol, n-propanol and isopropanol)
• Determination and correlation of solubility of 11alpha,17alpha-dihydroxy-4-pregnene-3,20-dione in different solvents
• Solubility determination and modelling of 4-nitro-1,2-phenylenediamine in eleven organic solvents from T = (283.15 to 318.15) K and thermodynamic properties of solutions
• Solubility determination and thermodynamic modelling for 2-amino-4-chlorobenzoic acid in eleven organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
• Liquid-liquid equilibrium measurements and correlation for phase behaviors of alcohols + heptane + ILs ternary systems
• Solubility determination and thermodynamic functions of 2-chlorophenothiazine in nine organic solvents from T = 283.15 K to T = 318.15 K and mixing properties of solutions
• Solubility and thermodynamic functions of tebuconazole in nine organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
• Influence of the temperature on the (liquid + liquid) phase equilibria of (water + 1-propanl + linalool or geraniol)
• Solubility of 2-isopropylimidazole in nine pure organic solvents and liquid mixture of (methanol + ethyl acetate) from T = (278.15 to 313.15) K: Experimental measurement and thermodynamic modelling
• Excess molar enthalpies of ethane-1,2-diamine plus primary and secondary alkanols (C1-C4) and correlation with Redlich-Kister, Wilson, NRTL and UNIQUAC models at T = 298 K
• Solubility of 2-nitro-p-phenylenediamine in nine pure solvents and mixture of (methanol + N-methyl-2-pyrrolidone) from T = (283.15 to 318.15) K: Determination and modelling
• Solubility of 4-methyl-2-nitroaniline in fourteen organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
• Solubility determination and thermodynamic modelling of 3,5-dimethylpyrazole in nine organic solvents from T = (283.15 to 313.15) K and mixing properties of solutions
• Thermodynamic functions for solubility of 3-nitro-o-toluic acid in nine organic solvents from T = (283.15 to 318.15) K and apparent thermodynamic properties of solutions
• Comparative study of physical properties of binary mixtures of halogen free ionic liquids with alcohols
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
• Measurement and correlation of (vapour-liquid) equilibrium for binary mixtures composed of 1-(ethoxymethoxy)-propane with ethanol and 1-propanol at 101.33 kPa
• Thermodynamic properties of enantiotropic polymorphs of glycolide
• Thermodynamic study of solubility for pyrazinamide in ten solvents from T = (283.15 to 323.15) K
• Solubility modelling and dissolution properties of 5-phenyltetrazole in thirteen mono-solvents and liquid mixtures of (methanol + ethyl acetate) at elevated temperatures
• Solubility modelling and preferential solvation of paclobutrazol in cosolvent mixtures of (ethanol, n-propanol and 1,4-dioxane) + water
• Thermodynamic functions for solubility of 2-mercaptobenzothiazole in eleven pure organic solvents at temperatures from 273.15 K to 318.15 K and mixing properties of solutions
• Solubility modelling, solution thermodynamics and preferential solvation for nitroxoline in solvent mixtures of ethyl acetate + (methanol, ethanol, n-propanol and isopropanol)
• Solubility and preferential solvation of 2-methyl-4-nitroaniline in mixed solvents of ethyl acetate + (methanol, ethanol, n-propanol and isopropanol)
• Isobaric vapor-liquid equilibria for the 1-propanol + water + 1-ethyl-3-methylimidazolium dicyanamide system at 100 kPa
• Physical properties of systems of interest to the edible oil industry: Viscosities and densities of model systems formed by (triacylglycerol + fatty acid + solvent)
• Isobaric vapor-liquid equilibria for extractive distillation of 1-propanol + water mixture using thiocyanate-based ionic liquids
• Thermodynamics and activity coefficients at infinite dilution for organic compounds and water in the ionic liquid 1-butyl-3-methylimidazolium perchlorate
• Excess molar volume and excess Gibbs energy of activation for viscous flow for the binary mixtures of N-ethylpyridinium dicyanamide [C2py][DCA] with alcohols
• Thermodynamic modelling of solubility and preferential solvation for ribavirin (II) in co-solvent mixtures of (methanol, n-propanol, acetonitrile or 1,4-dioxane) + water
• Separation of water/butan-1-ol based on activity coefficients at infinite dilution in 1,3-didecyl-2-methylimidazolium dicyanamide ionic liquid
• Estimation and confirmation of the thermodynamic stability relationships of the enantiotropic polymorphs of glycolide
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on gamma infinity data measurements
• Thermophysical properties of binary mixtures of 1-butyl-1-methylpyrrolidinium trifluoromethanesulfonate ionic liquid with alcohols at several temperatures
• Separation of binary mixtures based on gamma infinity data using [OMMIM][NTf2] ionic liquid and modelling of thermodynamic functions
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid trihexyl-tetradecyl-phosphonium tricyanomethanide
• Thermodynamic study of molecular interaction-selectivity in separation processes based on limiting activity coefficients
• Temperature and composition dependence of the volumetric and acoustic properties of ionic liquid [emim][HSO4] with polar protic and aprotic co-solvents
• Equilibrium solubility and preferential solvation of 1,1'-sulfonylbis(4-aminobenzene) in binary aqueous solutions of n-propanol, isopropanol and 1,4-dioxane
• Thermophysical and volumetric study of mixtures {p-cymene + propan-1-ol} at several temperatures and atmospheric pressure. Modeling with COSMO-RS
• Abraham model correlations for describing the thermodynamic properties of solute transfer into pentyl acetate based on headspace chromatographic and solubility measurements
• Solubility of l-tyrosine in aqueous solutions of methanol, ethanol, n-propanol and dimethyl sulfoxide: Experimental determination and preferential solvation analysis
• Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in ionic liquid [HMMIM][BF4]
• Electrostriction of water and lower alcohols around ammonium nitrate - Volumetric approach
• Thermodynamic evidence for nano-heterogeneity in solutions of the macrocycle C-butylresorcin[4]arene in non-aqueous solvents
• Intermolecular interactions in binary mixtures of 2-diethylethanolamine with 1-propanol and 1-butanol at different temperatures
• Thermodynamic behaviour of alkyl lactate-alkanol systems
• The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
• Solubility modelling, solvent effect and preferential solvation of carbendazim in aqueous co-solvent mixtures of N,N-dimethylformamide, methanol, ethanol and n-propanol
• The molar surface Gibbs energy and its application to the binary mixtures of N-butylpyridinium dicyanamide [C4py][DCA] with alcohols
• Thermodynamics and activity coefficients at infinite dilution for organic compounds in the ionic liquid 1-hexyl-3-methylimidazolium chloride
• Density, speed of sound and refractive index of mixtures containing 2-phenoxyethanol with propanol or butanol at various temperatures
• Separation of binary mixtures based on gamma infinity data using [OMMIM][BF4] ionic liquid and modelling of thermodynamic functions
• Solubility of dibenzothiophene in nine organic solvents: Experimental measurement and thermodynamic modelling
• Determination of the thermodynamic parameters of ionic liquid 1-propyl-3-methylimidazolium bromide by gas-liquid chromatography
• Thermodynamic solubility modeling, solvent effect and preferential solvation of curcumin in aqueous co-solvent mixtures of ethanol, n-propanol, isopropanol and propylene glycol
• The dissolution behavior and apparent thermodynamic analysis of temozolomide in pure and mixed solvents
• Mass density, sound velocity, mixing enthalpy, 1H NMR, Ab initio calculations and intermolecular interactions in binary mixtures of N-methylimidazole + water, +methanol, +ethanol, +1-propanol, +2-propanol
• Solubility modelling and thermodynamic aspect of 2,3-dihydro-6-propyl-2-thioxo-4(1H)-pyrimidinone in binary aqueous solutions of several alcohols
• Equilibrium solubility of dinitolmide in several neat solvents and binary aqueous co-solvent mixtures: Experimental determination and thermodynamic analysis
• Measurement and correlation of solubility of methyleneaminoacetonitrile in pure and binary solvents and thermodynamic properties of solution
• Volumetric properties of monoethanolamine and alcohol binary mixtures at different temperatures and 0.1 MPa
• Research on the application of 7-chloro-quinaldine adducts in 7-chloro-quinaldine separation process
• Determination and correlation of solubility and solution thermodynamics of saccharin in different pure solvents
• Thermodynamic and spectroscopic study of binary mixtures containing {dimethyl carbonate (DMC) + alcohols} at T = (288.15-308.15) K and p = (0.1-40) MPa: Experimental study and modelling
• Thermodynamic solubility modelling, solvent effect and preferential solvation of naftopidil in aqueous co-solvent solutions of (n-propanol, ethanol, isopropanol and dimethyl sulfoxide)
• Excess volumes and partial molar volumes of binary liquid mixtures of furfural or 2-methylfuran with alcohols at 298.15 K
• Surface tension and interfacial compositions of binary glycerol/alcohol mixtures
• Separation of the mixture (isopropyl alcohol + diisopropyl ether + n-propanol): Entrainer selection, interaction exploration and vapour-liquid equilibrium measurements
• Cosolvent effect on solubility of aripiprazole in mixed solvents and apparent thermodynamic analysis of dissolution process
• Research and comparison of solid-liquid phase equilibrium and ternary phase diagrams of 1-(3-nitrophenyl)ethanone + 1-(4-nitrophenyl)ethanone in different solvents
• Effect of temperature on the phase-separation ability of KCl in aqueous two-phase systems composed of propanols: Determination of the critical temperature and extension of the results to other salts
• Separation of (water/butan-1-ol) binary systems based on activity coefficients at infinite dilution with phosphonium ionic liquid
• The dissolution behaviour and apparent thermodynamic analysis of diprophylline in pure and mixed solvents
• Co-solvence phenomenon and thermodynamic properties of edaravone in pure and mixed solvents
• Improving the solubility of temozolomide by cosolvent and its correlation with the Jouyban-Acree and CNIBS/R-K models
• Volumetric, acoustic and viscometric investigation of ceftriaxone disodium in aqueous solutions of 1-propanol and 2-propanol
• Experimental studies on the thermal conductivity of methyl laurate component of biodiesel with three alcohols
• Solubility and mixing thermodynamic properties of levamisole hydrochloride in twelve pure solvents at various temperatures
• Vapor-liquid equilibrium and excess properties of the binary mixtures formed by ethyl isobutyrate and n-alkanols
• Excess molar enthalpies of methyl isobutyl ketone (MIBK) with alkan-1-ols (C1-C6) and their correlations at 298.15 K
• Molar excess enthalpies of ethyl acetate + alkanols at T=298.15K, p=10MPa
• Ternary excess molar enthalpies of (1-propanol + 2-propanol + 1,4-dioxane) mixture at 298.15 K
• Excess molar enthalpies of methylformate + (1-propanol, 2-propanol, 1-butanol, 2-butanol and 1-pentanol) at T = 298.15 K, p = (5.0, 10.0)MPa, and methylformate + 1-propanol at T = 333.15 K, p = 10.0MPa
• Construction of solid liquid phase diagrams in ternary systems by titration calorimetry
• Excess enthalpies of binary mixtures of some propylamines + some propanols at 298.15K
• Excess molar enthalpies and heat capacities of dimethyl sulfoxide + seven normal alkanols at 303.15K and atmospheric pressure
• Thermodynamic properties of binary mixtures of 2.2.2-Trifluoroethanol with Water or Alkanols at T=298.15 K
• Enthalpies of dilution of formamide in aqueous alcohol solutions at 298.15K
• Excess molar enthalpies for binary mixtures of trimethyl phosphate with alkanols {CH3(CH2)nOH, n = 0 3} at 298.15K
• 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
• Topological investigations of the molecular species and molecular interactions that characterize pyrrolidin-2-one + lower alkanol mixtures
• Excess molar volumes of Diisopropylamine + (C1-C5) Alkan-1-ols: application of the ERAS model and cubic EOS
• Experimental Determination and Modeling of Densities and Refractive Indices of the Binary Systems Alcohol + Dicyclohexylamine at T = (288.15 to 323.15) K
• Thermodynamic Study of Binary Mixture of x1[C6mim][BF4] + x21-propanol: Measurements and Molecular Modeling
• Solubilities of 1,3-dimethyl-1,1,3,3-tetraphenyldisiloxane in different solvents from (288.15 to 313.15) K
• Liquid-Liquid Equilibrium of Aqueous Two-Phase Systems Composed of Hydrophilic Alcohols (Ethanol/2-Propanol/1-Propanol) and MgSO4 /ZnSO4 at (303.15 and 313.15) K and Correlation
• Thermodynamic behavior of binary mixtures CnMpyNTf2 ionic liquids with primary and secondary alcohols
• Molar excess enthalpies and molar excess volumes of formamide + 1-propanol or 2-propanol and thermodynamic modeling by Prigogine-Flory-Patterson theory and Treszczanowicz-Benson association model
• Experimental measurements and modelling of volumetric properties, refractive index and viscosity of selected binary systems with butyl lactate at 288.15 to 323.15 K and atmospheric pressure. New UNIFAC-VISCO interaction parameters.
• Liquid liquid equilibria of hydrophilic alcohol + sodiumhydroxide + water systems: Experimental and correlation
• THERMODYNAMICS OF MIXTURES CONTAINING AMINES. XIV. CpEm OF BENZYLAMINE WITH HEPTANE AT 293.15 K OR WITH METHANOL, 1-PROPANOL OR 1-PENTANOL AT (293.15-308.15) K
• Excess volumes, Viscosities, and Excess Gibbs Energy of Activation for Viscous Flow, for binary and ternary mixtures 1- propanol + N-N dimethylformamid + chloroform at different temperatures
• Mutual diffusion behavior of short chain alcohols + n-octane mixtures
• Measurement and correlation of the solubility of (1-benzyl-1H-1,2,3-triazole-4-yl)methanol in water and alcohols at temperatures from 292.15 K to 310.15 K
• Measurement and correlation of solubility of carbendazim in lower alcohols
• The excess molar volume and the molar surface Gibbs energy of the binary of the ether-functionalized ionic liquids [C22O1IM][TfO] with ethanol and isomeric propanols at T = (288.15-318.15) K
• Modified Method for Measuring the Solubility of Pharmaceutical Compounds in Organic Solvents by Visual Camera
• Experimental and Computational Thermodynamic Properties of (Benzyl alcohol + Alkanols) Mixtures
• Density, Viscosity, and Sound Speed of Bis(trifluoromethylsulfonyl)imide-Based Ionic Liquids + 1-Propanol Mixtures
• Liquid-Liquid Equilibrium of Alcohols + Ammonium/Potassium/Sodium Acetate + Water Systems: Experimental and Correlation
• Densities and Viscosities of Binary Mixtures of 2-Ethyl-1,1,3,3- tetramethylguanidinium Ionic Liquids with Ethanol and 1-Propanol
• Lamotrigine Solubility in Some Nonaqueous Solvent Mixtures at 298.2 K
• Vapor-Liquid Equilibrium of Binary Mixtures Containing Isopropyl Acetate and Alkanols at 101.32 kPa
• Thermodynamic Analysis of the Experimental Equilibria for the Liquid-Phase Etherification of Isobutene with C1 to C4 Linear Primary Alcohols
• Solubility and Dissolution Thermodynamics for 1,3,5- Trichlorobenzene in Organic Solvents
• Measurement and Correlation of the Solubility of Vanillic Acid in Eight Pure and Water + Ethanol Mixed Solvents at Temperatures from (293.15 to 323.15) K
• Solubility of Hydrogen Sulfide in Ethanediol, 1,2-Propanediol, 1-Propanol, and 2-Propanol: Experimental Measurement and Modeling
• Solubility Measurement and Modeling of 4,4'-Dihydroxydiphenyl Sulfone in Nine Organic Solvents from T = (278.15 to 313.15) K and Thermodynamic Property of Dissolution
• Solubility of Benzoic Acid and Aspirin in Pure Solvents Using Focused Beam Reflective Measurement
• Thermodynamic Models for Determination of the Solubility of Boc-(R)-3-Amino-4-(2, 4, 5-trifluorophenyl)butanoic acid in Different Pure Solvents and (Tetrahydrofuran + n-Butanol) Binary Mixtures with Temperatures from 280.15 to 330.15 K
• Liquid-Liquid Equilibrium of Hydrophilic Alcohols with Three Different Salts of Chloride: Experimental and Correlation
• Liquid-Liquid Equilibria for Ternary Systems of Water + Methoxycyclopentane (CPME) + Alcohol; Methanol, Ethanol, 1-Propanol, or 2-Propanol
• Solid Liquid Phase Equilibrium of trans-Cinnamic Acid in Several Alcohols: Measurements and Thermodynamic Modeling
• Measurement and Correlation of the Solubility of Antioxidant 626 in Alcohols
• Measurement and Correlation of Solubility of -Aminobutyric Acid in Different Binary Solvents
• Thermodynamics of 1,3-dimethylurea in eight alcohols
• Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
• Measurements of Infinite Dilution Activity Coefficients of Alkanols in the Ionic Liquid Tributylmethylammonium Methyl Sulfate Using HS-SPME/GC/FID
• Experimental Measurement and Modeling of Vapor-Liquid Equilibrium for the Ternary System Water + 1-Propanol + Glycerol
• Thermophysical Characterization of the Mixtures of the Ionic Liquid 1-Ethyl-3-Methylimidazolium Acetate with 1-Propanol or 2-Propanol
• Indirect Analysis of a Homogeneous Ternary Mixture
• Solubility Modeling of 4-(Methylsulfonyl)benzaldehyde in Nine Organic Solvents at Elevated Temperatures
• Solubility of Ethyl p-Aminobenzoate in Six Alcohols within (283.15 to 327.15) K
• Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
• Experimental Measurement and Modeling of Vapor Liquid Equilibrium for the Ternary Systems Water + Ethanol + Ethylene Glycol, Water + 2-Propanol + Ethylene Glycol, and Water + 1-Propanol + Ethylene Glycol
• Solubility of 3,7,9,11-Tetraoxo-2,4,6,8,10-pentaaza[3.3.3] Propellane (TOPAP) in Different Pure Solvents at Temperatures between 273.15 and 318.15 K
• Measurement and Correlation of the Solubility of p-Coumaric Acid in Nine Pure and Water + Ethanol Mixed Solvents at Temperatures from 293.15 to 333.15 K
• Measurement and Correlation of Solubility on Reactive Crystallization of Methyl D-(-)-4-Hydroxy-phenylglycinate
• Liquid Liquid Equilibria of Quaternary Systems Composed of 1,3-Propanediol, Short-Chain Alcohol, Water, and Salt
• Liquid Liquid Equilibria of the Water + 1-Propanol + 1-Butyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ternary System: Study of the Ability of Ionic Liquid as a Solvent
• Activity and Osmotic Coefficients of Binary Mixtures of NTf2 Ionic Liquids with a Primary Alcohol
• Physical Properties of the Pure Deep Eutectic Solvent, [ChCl]:[Lev] (1:2) DES, and Its Binary Mixtures with Alcohols
• Solubility of 4-Methylsulfonylacetophenone in Nine Pure Solvents and (Ethyl Acetate + n-Hexane) Binary Solvent Mixtures from 278.15 K to 328.15 K
• Solubility Correlation and Thermodynamic Analysis of Sorafenib Free Base and Sorafenib Tosylate in Monosolvents and Binary Solvent Mixtures
• Solubility and Thermodynamic Behavior of Veramoss in Different Pure Solvents and {Ethanol + Water} Mixtures from T = 283.15 to 333.15 K
• Measurement and Correlation of Solubility of Loratadine in Different Pure Solvents and Binary Mixtures
• Isobaric Vapor Liquid Liquid Phase Equilibria Measurements of Three Ternary Water + 2-Butanone + Aliphatic Alcohol (Ethanol, 1-Propanol, 2-Propanol) Systems at 101.3 kPa
• 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
• Determination of Ternary Liquid Liquid Equilibria for Dimethyl Carbonate + 2-Methyl-1-propanol or 2-Methyl-2-propanol + Water Systems at T = 303.15 and 313.15 K
• Ternary Liquid Liquid Equilibrium of Azeotropes (Ester + Alcohol) with Different Ionic Liquids at T = 298.15 K
• Solubilities of 4',5,7-Triacetoxyflavanone in Fourteen Organic Solvents at Different Temperatures
• Phase Separation of Alcohol (1-Propanol, 2-Propanol, or tert-Butanol) from Its Aqueous Solution in the Presence of Biological Buffer MOPS
• Measurement and Correlation of the Solubility of 2,6-Dihydroxybenzoic Acid in Alcohols and Binary Solvents
• Volumetric Properties of Sodium Lauroylsarcosinate in Aqueous Alcohol Solutions of Methanol, Ethanol, and 1-Propanol
• Vapor Liquid Equilibrium for Methyl Isobutyl Ketone (MIBK) + (1-Propanol or 2-Propanol) Binary Mixtures
• Measurement and Correlation of Solubility of Theobromine, Theophylline, and Caffeine in Water and Organic Solvents at Various Temperatures
• Isobaric Vapor Liquid Equilibrium for the Binary Systems Dimethyl Disulfide + C1 C4 n-Alkanol at 40.000 and 101.325 kPa
• Proposal of Isobutyl Alcohol as Entrainer To Separate Mixtures Formed by Ethanol and Water and 1-Propanol and Water
• Influence of Temperature on the Liquid Liquid Phase Equilibria of Ternary (Water + Alcohol + Entrainer) Systems
• Pressurized-Synthetic Methodology for Solubility Determination at Elevated Temperatures with Application to Paracetamol in Pure Solvents
• Solid Liquid Phase Equilibrium of N,N'-Piperazinebis(neopentylglycol)phosphoramidate in Selected Solvents from T = (293.15 to 333.15) K
• Solubility of Benzoin in Six Monosolvents and in Some Binary Solvent Mixtures at Various Temperatures
• Solubility Determination and Thermodynamic Modeling of Sodium Thioglycolate in Pure and Binary Solvent Mixtures from T = (293.15 to 333.15) K
• Volumetric Properties, Viscosity, and Refractive Indices of Different Naringenin Solutions at Several Temperatures
• Measurement and Correlation of Solubility of Two Isomers of Cyanopyridine in Eight Pure Solvents from 268.15 K to 318.15 K
• Thermodynamic Functions for Solubility of 1-Hydroxybenzotriazole in Sixteen Solvents at Temperatures from (278.15 to 313.15) K and Mixing Property of Mixtures
• Study on the Solubilities of Mononitro-Substituted Products of Nitration of m-Toluic Acid in Several Solvents at Temperatures between 297.65 and 351.75 K
• Isobaric Vapor-Liquid Equilibrium for the Binary Systems of Sec-butyl Acetate and Ethanol, 1-Propanol, or 2-Propanol at 101.3 kPa
• Ammonium-Based Ionic Liquid as an Entrainer for the Separation of n-Propanol + Water and Isopropanol + Water Mixtures
• Solubility Modeling and Mixing Thermodynamics of Thiamphenicol in Water and Twelve Neat Organic Solvents from T = (278.15 to 318.15) K
• Solid-Liquid Equilibria for the Glycine-Alcohol-NaCl-H2O System
• Measurement and Correlation of Activity, Density, and Speed of Sound for Binary Mixtures of 1-Propanol + Poly(Propylene Glycol) 400, 725, and 1025
• 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
• Separation of Azeotropes Hexane + Ethanol/1-Propanol by Ionic Liquid Extraction: Liquid-Liquid Phase Equilibrium Measurements and Thermodynamic Modeling
• Determination and Correlation of Solubility and Thermodynamic Properties of trans-Cinnamyl Alcohol in Pure and Binary Solvents from 253.15 K to 293.15 K
• Measurement and Correlation of the Solubility of Azoxystrobin in Seven Monosolvents and Two Different Binary Mixed Solvents
• Measurement and Correlation of Solubility of Resorcinol Bis(cyclic 2,2-dimethyl-1,3-propanediol phosphate) in Selected Solvents from T = 293.15 to 333.15 K
• Solubility and Mixing Thermodynamics Properties of p-Toluenesulfonamide and o-Toluenesulfonamide in Seven Monosolvents at Different Temperatures
• Three Binary Azeotropic Systems for 1-(Methoxymethoxy)-propane, 1-(Ethoxymethoxy)-propane, and Methoxy(methoxymethoxy)methane with Three Alcohols at 101.33 kPa: Experimental Data, Correlation, and Purification
• Solubility Modeling and Mixing Properties for Benzoin in Different Monosolvents and Solvent Mixtures at the Temperature Range from 273.15 to 313.15 K
• The Solid-Liquid Equilibrium and Crystal Habit of l-Carnitine Fumarate
• Determination and Correlation of Dipyridamole p-Toluene Sulfonate Solubility in Seven Alcohol Solvents and Three Binary Solvents
• Solubility and Modeling of Hesperidin in Cosolvent Mixtures of Ethanol, Isopropanol, Propylene Glycol, and n-Propanol + Water
• Solubility of p-Aminobenzoic Acid Potassium in Organic Solvents and Binary (Water + Isopropyl Alcohol) Mixture at Temperatures from (283.15 to 318.15) K
• Solubility and Preferential Solvation of Carbazochrome in Solvent Mixtures of N,N-Dimethylformamide Plus Methanol/Ethanol/n-Propanol and Dimethyl Sulfoxide Plus Water
• Aniracetam Solubility in Pure and Binary Solvents: Effect of Molecular Interaction and Analysis of Crystallized Products
• Isobaric Vapor-Liquid Phase Equilibrium Measurements, Correlation, and Prediction for Separation of the Mixtures of Cyclohexanone and Alcohols
• Measurement and Correlation of the Solubility of Florfenicol Form A in Several Pure and Binary Solvents
• Densities and Excess Molar Volumes for the Binary and Ternary Systems of (1,4-Dioxane, 1-Propanol or 2-Propanol, and 1,2-Dichloroethane) at T = (288.15 to 318.15) K. Experimental Measurements and Prigogine-Flory-Patterson Modeling
• 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
• Solubility of 2-Chlorophenylacetic Acid in 12 Pure Solvents from T = (273.15/283.15 to 318.15) K: Determination and Modeling
• Experimental Determination and Thermodynamic Models for Solid-Liquid Equilibrium of 4-(4-Aminophenoxy)-N-methylpyridine-2-carboxamide in Pure and Binary Solvent Mixtures for T = (278.15-328.15) K
• Determination of Physicochemical Parameters of Sodium Dodecyl Sulfate in Aqueous Micellar Solutions Containing Short-Chain Alcohols
• Measurement and Modelization of VLE for Butyl Acetate with Methanol, Ethanol, 1-Propanol, and 1-Butanol. Experimental Data at 0.15 MPa
• 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
• Determination of Solubility and Thermodynamic Properties of Benzophenone in Different Pure Solvents
• Solubility and Molecular Interactions of Trimetazidine Hydrochloride in 12 Monosolvents and Solvent Mixtures of Methanol + (Ethanol, N,N-Dimethylformamide or Ethyl Acetate)
• Cosolvency and Mathematical Modeling Analysis of Chloroxine in Some Binary Solvent System
• Research on Dissolution Capability of Several Antofloxacin Salts
• Solubility Measurement and Modeling of 2-Amino-4,6-dichoropyrimidine in Ten Pure Solvents and (Ethyl Acetate + Ethanol) Solvent Mixtures
• Liquid-Liquid Extraction of Alcohols from Their Azeotropic Mixtures with Hexane Using Ionic Liquid
• Measurement and Correlation of the Solubility of 5-Fluorouracil in Pure and Binary Solvents
• 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
• Density, Viscosity, and Speed of Sound of Pure and Binary Mixtures of Ionic Liquids Based on Sulfonium and Imidazolium Cations and Bis(trifluoromethylsulfonyl)imide Anion with 1-Propanol
• Thermodynamic Study of Solubility for Imatinib Mesylate in Nine Monosolvents and Two Binary Solvent Mixtures from 278.15 to 318.15 K
• P-rho-T Data and Modeling for Propan-1-ol + n-Octane or n-Nonane or n-Decane from 313.15 K to 363.15 K and 1 MPa to 20 MPa
• Solubility Determination and Modeling for 4-Nitrobenzonitrile in Binary Solvent Mixtures of Ethyl Acetate Plus (Methanol, Ethanol, n-Propanol, and Isopropanol)
• Solubility Determination of Nicotinamide and Its Application for the Cocrystallization with Benzoic Acid
• Solubility Measurements at 296 and 310 K and Physicochemical Characterization of Abiraterone and Abiraterone Acetate
• Measurement and Correlation of Solubility of 3-Hydroxy-2-naphthoic Acid in Ten Pure and Binary Mixed Organic Solvents from T = (293.15 to 333.15 K)
• 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
• Vapor-Liquid Equilibrium, Volumetric, and Compressibility Properties of 1-Propanol + Poly(ethylene glycol) Dimethyl Ether 250 and 500 Binary Mixtures
• Measurement and Correlation of Solubility and Thermodynamic Properties of Vinpocetine in Nine Pure Solvents and (Ethanol + Water) Binary Solvent
• Solubility Determination and Correlation of Glibenclamide in 11 Monosolvents and (Acetone + Acetonitrile) Binary Solvents from 283.15 K to 323.15 K
• Solubility Measurement and Thermodynamic Properties of Levetiracetam in Pure and Mixed Solvents
• Solution Thermodynamic Analysis of p-(Aminomethyl)benzoic Acid in Four Binary Solvents from 288.15 to 328.15 K
• Liquid-Liquid Equilibrium Data for the Systems n-Propyl Acetate or Isopropyl Acetate + n-Propanol or Isopropyl Alcohol + IL at 298.15 and 318.15 K and Atmospheric Pressure
• Solid-Liquid Equilibrium of Rebaudioside A in Pure and Binary Mixed Solvents at T = (288.15 to 328.15) K
• Solubility and Data Correlation of Isoniazid in Different Pure and Binary Mixed Solvent Systems from 283.15 K to 323.15 K
• Solubility Measurement and Correlation of Probenecid in 12 Pure Organic Solvents and Thermodynamic Properties of Mixing of Solutions
• Measurement and Correlation of the Solubility of Tetramethylpyrazine in Nine Monosolvents and Two Binary Solvent Systems
• Measurement and Correlation of Solubility of Gatifloxacin in 12 Pure Solvents from 273.15 K to 318.15 K
• Solubility Measurement and Thermodynamic Model Correlation and Evaluation of 2-Chloro-5-nitroaniline in 12 Pure Solvents
• Atmospheric Ternary Liquid-Liquid Equilibrium for the Diethyl Carbonate + 1-Propanol + Water System at Temperature of 303.15, 313.15, 323.15, and 333.15 K
• Thermodynamic Speed of Sound Data for Liquid and Supercritical Alcohols
• Effect of the Alkyl Chain on the Physical Properties of Imidazolium-Based Ionic Liquids with 1-Propanol, 1-Butanol, and 1-Pentanol Binary Mixtures
• Density and Derived Properties of Binary Mixtures Containing {2-(Dimethylamino)ethyl Methacrylate + Alcohols} at Temperatures from T = (293.15 to 313.15) K and Pressures of up to 35 MPa
• Solubility Modeling and Solvent Effect of 2-Amino-6-chloropurine in Twelve Neat Solvents
• Solubility Measurement of Lauric, Palmitic, and Stearic Acids in Ethanol, n-Propanol, and 2-Propanol Using Differential Scanning Calorimetry
• Equilibrium Solubility of Biapenem in Different Neat and Binary Solvents: Experimental Determination and Model Correlation
• Measurement and Correlation of the Solubility of Mifepristone in Eight Pure and Water + Methanol Mixed Solvents at Temperatures from 273.15 to 318.15 K
• Effect of Solvent Properties and Composition on the Solubility of Ganciclovir Form I
• Measurement and Modeling of Solid-Liquid Equilibria of l-Glutamic Acid in Pure Solvents and Aqueous Binary Mixtures
• Density and Viscosity of 2-Butanol + (1-Propanol, 2-Propanol, or 3-Amino-1-propanol) Mixtures at Temperatures of (293.15 to 323.15) K: Application of the ERAS Model
• Solubility Determination and Thermodynamic Modeling of Buprofezin in Different Solvents and Mixing Properties of Solutions
• Solubility in Different Solvents, Correlation, and Solvent Effect in the Solvent Crystallization Process of Iohexol
• Solubility Modeling and Solvent Effect for Flubendazole in 12 Neat Solvents
• Determination and Modeling of Solubility of 4-Aminobenzamide in Different Pure Solvents
• Binary Solid-Liquid Solubility Determination and Model Correlation of Quizalofop-p-ethyl in Different Pure Solvents
• Measurement and Correlation of the Solubility of Baicalin in Several Mixed Solvents
• Solid-Liquid Equilibrium of Azacyclotridecan-2-one in 15 Pure Solvents from T = 273.15 to 323.15 K: Experimental Determination and Thermodynamic Modeling
• Measurement and Correlation of the Solubility of 2-Cyanoacetamide in 14 Pure Solvents and the Mixing Properties of Solutions
• Solubility Determination of 1,5-Naphthalenediamine and 1,8-Naphthalenediamine in Different Solvents and Mixing Properties of Solutions
• Solubility, Model Correlation, and Solvent Effect of 2-Amino-3-methylbenzoic Acid in 12 Pure Solvents
• Solubility and Solution Thermodynamics of 3-Nitrophthalonitrile in 12 Neat Solvents at Temperatures from 278.15 to 323.15 K
• 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
• Equilibrium Solubility, Model Correlation, and Solvent Effect of Indole-3-acetic Acid in Twelve Pure Solvents
• 4-Nitrophenzylcyanide Solubility in Several Nonaqueous Solvent Mixtures: Determination and Modeling
• Measurement and Correlation of Solubility of Calcium Formate (Form alpha) in Different Binary Solvent Mixtures at Temperatures from 283.15 to 323.15 K
• Isobaric Vapor-Liquid Equilibrium of the Acetonitrile + 1-Propanol + Ionic Liquids at an Atmospheric Pressure
• 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 Modeling of p-Nitrobenzamide Dissolved in Twelve Neat Solvents from 283.15 to 328.15 K
• Solubility of Bifonazole in Four Binary Solvent Mixtures: Experimental Measurement and Thermodynamic Modeling
• Isothermal Vapor-Liquid Equilibrium Measurements for the Pentan-2-one + Propan-1-ol/Butan-1-ol System within 342-363 K
• Isothermal Vapor-Liquid Equilibrium Measurements for Alcohol + Water/n-Hexane Azeotropic Systems Using Both Dynamic and Automated Static-Synthetic Methods
• Liquid Densities and Speed of Sound for Ionic Liquid (2-HEAA and 2-HDEAA) + Alcohol (1-Propanol and 2-Propanol) Mixtures at T = (293.15-323.15 K) and Atmospheric Pressure
• Solid-Liquid Equilibrium Measurements for Posaconazole and Voriconazole in Several Solvents between T = 278.2 and 323.2 K Using Differential Thermal Analysis/Thermal Gravimetric Analysis
• Solubility Determination and Thermodynamic Modeling of 2-Mercaptobenzimidazole in 12 Solvents from T = 278.15 K to T = 318.15 K
• Measurement and Correlation of Solubility of Hydrochlorothiazide in Monosolvents and Binary Solvent Mixtures from 283.15 to 323.15 K
• Solubility Measurement and Thermodynamic Model Correlation of 5-Nitrosalicylaldehyde in Different Solvents
• o-Nitrophenylacetonitrile Solubility in Several Pure Solvents: Measurement, Correlation, and Solvent Effect Analysis
• Solubility of d-Tryptophan and l-Tyrosine in Several Organic Solvents: Determination and Solvent Effect
• Solubility of Gastrodin in Pure and Mixed Solvents at 273.15-313.15 K and Its Correlation with Different Thermodynamic Models
• Solubility Measurement and Correlation of 2-Oxindole in 12 Pure Organic Solvents
• Solubility of d-Aspartic Acid in Several Neat Solvents: Determination, Modeling, and Solvent Effect Analysis
• Assessment of Pyrrolidinium-Based Ionic Liquid for the Separation of Binary Mixtures Based on Activity Coefficients at Infinite Dilution
• Solubility Measurement and Phase Equilibrium Modeling of 2-Aminobenzamide in 15 Pure Solvents
• Measurement of the Solubility of Diclazuril and Discussion of the Effect of the Cosolvent
• Solubility Determination, Modeling, and Thermodynamic Dissolution Properties of Benzenesulfonamide in 16 Neat Solvents from 273.15 to 324.45 K
• Solid-Liquid Equilibrium Solubility, Thermodynamic Properties, and Molecular Simulation of Phenylphosphonic Acid in 15 Pure Solvents at Different Temperatures
• Determination and Correlation of Solubilities of 1,3,5-Trifluoro-2,4,6-triiodobenzene in Different Solvents from 289.25 to 332.15 K
• Solubility Determination, Correlation, and Solute-Solvent Molecular Interactions of 5-Aminotetrazole in Various Pure Solvents
• Solubility Determination and Thermodynamic Mixing Properties of 5-Methyl-2-pyrazinecarboxylic Acid in Different Solvents
• Solubility and Thermodynamic Modeling of Sulfanilamide in 12 Mono Solvents and 4 Binary Solvent Mixtures from 278.15 to 318.15 K
• Solubility Determination and Modeling of EGCG Peracetate in 12 Pure Solvents at Temperatures from 278.15 to 318.15 K
• Solubility Measurement and Thermodynamic Modeling for o-Toluenesulfonamide in 16 Solvents from T = 273.15 to 323.85 K
• Binary Equilibrium Solubility of Amidinothiourea in Monosolvents: Experimental Determination, Model Correlation, and Solvent Effect Analysis
• Measurement and Correlation of Solubility of Marbofloxacin in 12 Pure Solvents from 283.15 to 328.15 K
• 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
• Solubility Measurement and Modeling of 3-Hydroxy-2-nitropyridine in Ten Pure Solvents and Two Binary Mixed Solvents for T = (278.15-318.15) K
• Solubility of Acetoguanamine in Twelve Neat Solvents from 283.15 to 323.15 K
• Solubility and Thermodynamic Modeling of Dimethyl Terephthalate in Pure Solvents and the Evaluation of the Mixing Properties of the Solutions
• 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
• Measurement and Correlation of the Solubility of Dienogest in Twelve Pure and Water + Methanol Binary Solvents at Temperatures from 273.15 to 318.15 K
• Solubility and Data Correlation of b-Arbutin in Different Monosolvents from 283.15 to 323.15 K
• 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 Solubility and Mixing Properties of Phenformin in 14 Pure Solvents at Temperatures Ranging from 278.15 to 323.15 K
• Solid-Liquid Phase Equilibrium and Thermodynamic Analysis of N,N'-Diethylthiourea in Different Solvent Systems
• Thermodynamic Solubility of Gatifloxacin in Nonaqueous Solvent Mixtures of N,N-Dimethylformamide Plus Isopropanol/Methanol/n-Propanol/Ethanol
• Isobaric Phase Equilibria of Diethyl Carbonate with Five Alcohols at 101.3 kPa
• Excess Molar Enthalpies for Binary Mixtures of Ethanol + Acetone, + Octane, + Cyclohexane and 1-Propanol + Acetone, + Octane, + Heptane at 323.15
• Solubility of Anthracene in Binary Alcohol + Acetonitrile Solvent Mixtures at 298.2 K
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 3. Liquid-Liquid Equilibria of Binary Mixtures of 1-Ethyl-3-methylimidazolium Bis(trifluoromethylsulfonyl)imide with Propan-1-ol, Butan-1-ol, and Pentan-1-ol
• Solubility in Binary Solvent Mixtures: Pyrene Dissolved in Alcohol + Acetonitrile Mixtures at 299.2 K
• Solubility of Benzimidazoles in Alcohols
• VLE and VLLE Measurements of Dimethyl Ether Containing Systems. 2
• Bubble Temperatures of the Binary Mixtures of Dimethylcarbonate with Some Alcohols at 95.8 kPa
• Speed of Sound in Propan-1-ol + Heptane Mixtures under Elevated Pressures
• Solubility in Binary Solvent Mixtures: Anthracene Dissolved in Alcohol + 2-Methyl-1-butanol Mixtures at 298.2 K
• Solubility in Binary Solvent Mixtures: Anthracene Dissolved in Alcohol + Carbon Tetrachloride Mixtures at 298.2 K
• Measurement and Correlation of Excess Molar Enthalpies for Ethylene Glycol + Alkanol Systems at the Temperatures (298.15, 308.15, and 323.15) K
• Excess Molar Volumes, Viscosities, and Refractive Indexes for Binary Mixtures of 1-Chlorobutane with Four Alcohols at T = (288.15, 298.15 and 308.15) K
• Limiting Activity Coefficients by Comparative Tensimetry: 1-Propanol and 1-Butanol in Heptane and in Octane
• Density, Surface Tension, and Refractive Index of Octane + 1-Alkanol Mixtures at T ) 298.15 K.
• Isochoric Heat Capacities of Alkanols and Their Aqueous Mixtures
• Dynamic Viscosities of Diethyl Carbonate with Linear and Secondary Alcohols at Several Temperatures
• Thermochemistry of Branched Ethers: Experimental Study of Chemical Equilibrium in the Reacting System of tert-Amyl Alkyl Ether Synthesis
• Vapor-Pressure Measurements of Liquid Solutions at Different Temperatures: Apparatus for Use over an Extended Temperature Range and Some New Data
• Densities and Viscosities of Binary Liquid Mixtures of Trichloroethylene and Tetrachloroethylene with Some Polar and Nonpolar Solvents
• Thermodynamic Investigation of the Azeotropic Binary Mixture Water + n-Propanol
• Excess Molar Volumes and Viscosity Deviations of Binary Mixtures of 2,4,6-Trimethyl-1,3,5-trioxane + Ethanol, 1-Propanol, and 1-Butanol at (298.15, 303.15, and 308.15) K
• Thermodynamic Properties of Mixtures Containing Ionic Liquids.4.LLE of Binary Mixtures of [C2MIM][NTf2] with Propan-1-ol, Butan-1-ol, and Pentan-1-ol and [C4MIM][NTf2] with Cyclohexanol and 1,2-Hexanediol Including Studies of the Influence of Small Amounts of Water
• Determination of Henry s Law Constants and Activity Coefficients at Infinite Dilution of Flavor Compounds in Water at 298 K with a Gas-Chromatographic Method
• Density Measurements under Pressure for the Binary System 1-Propanol + Toluene
• Measurement of Diffusion Coefficients in Thermodynamically Nonideal Systems
• Vapor-Liquid Equilibrium Behavior of Tolan in Alcohol
• Excess Molar Enthalpies of Ternary Mixtures of Ethanol + 1-Propanol + Tetrahydropyran or 1,4-Dioxane at 298.15 K
• Solubilities of Proxetine Hydrochloride Hemihydrate between 286 K and 363 K
• Viscosities, Densities, and Ultrasonic Velocities of Binary Mixtures of Ethylbenzene with Ethanol, 1-Propanol, and 1-Butanol at (298.15 and 308.15)K
• Solid - Liquid Phase Equilibrium of Some Aliphatic Alcohols + Cesium Sulfate + Water
• Vapor-Liquid Equilibrium for Benzene + 2-Methylpentane and Allyl Alcohol + 1-Propanol
• Vapor-Liquid Equilibrium for 1-Propanol + 1-Butene, + cis-2-Butene, + 2-Methyl-propene, + trans-2-Butene, + n-Butane, and + 2-Methyl-propane
• Solubility and Density of 2,6-Dimethylnaphthalene in C1-C7 1-Alkanols
• Heat Capacities and Derived Thermodynamic Functions of 1-Propanol between 10 K and 350 K and of 1-Pentanol between 85 K and 370 K
• Excess Enthalpy, Excess Volume, and Speed of Sound Deviation for the Mixtures ss-Pinene + Ethanol and ss-Pinene + 1-propanol at (283.15, 298.15 and, 313.15) K
• Surface Tension of Dilute Solutions of Linear Alcohols in Benzyl Alcohol
• Excess Molar Enthalpies of Dimethyl Carbonate and (Methanol, Ethanol, 1-Propanol, and 2-Propanol) at T = (298.15, 313.15, and 328.15) K and p = (0.1, 1.0, and 10.0) MPa
• Density and Viscosity of Binary Mixtures of Ethyl-2-methylbutyrate and Ethyl Hexanoate with Methanol, Ethanol, and 1-Propanol at (293.15, 303.15, and 313.15) K
• Solubility of Cesium Nitrate in Alcohol Aqueous Solutions at (25, 35 and 45 ) C
• Phase Diagrams of Some Aliphatic Alcohols + Potassium or Sodium Citrate + Water at 25 deg C
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 5. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Methyl-3-butyl-imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using Gas-Liquid Chromatography
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 6. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Methyl-3-octyl-imidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Solubility of Potassium Clavulanate in Ethanol, 1-Propanol, 1-Butanol, 2-Propanol, and 2-Methyl-1-propanol between 273 K and 305 K
• Densities, Viscosities, and Ultrasonic Velocity Studies of Binary Mixtures of Chloroform with Propan-1-ol and Butan-1-ol at (303.15 and 313.15) K
• Excess Molar Enthalpies of Methyl Acetate and (1-Propanol, 2-Propanol, 1-Butanol, 2-Butanol, and 1-Pentanol) at T = (298.15 and 308.15) K and P = (5.0 and 10.0) MPa
• Experimental and Predicted Results of Anomeric Equilibrium of Glucose in Alcohols
• Density, Refractive Index, Speed of Sound at 298.15 K, and Vapor-Liquid Equilibria at 101.3 kPa for Binary Mixtures of Propanol + 2-Methyl-1-butanol and Propanol + 3-Methyl-1-butanol
• Solubility of Cefazolin Sodium Pentahydrate in Different Solvents between 275 K and 310 K
• Equilibrium Phase Behavior of Water + Propan-1-ol or Propan-2-ol + Cesium Chloride at (298.15, 308.15, and 318.15) K
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 8. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography
• Vapor Pressures and Activity Coefficients of n-Alcohols and Benzene in Binary Mixtures with 1-Methyl-3-Butyl-Imidazolium Octylsulfate and 1-Methyl-3-Octyl-Imidazolium Tetrafluoroborate
• Isothermal Vapor Liquid Equilibrium for 2-Methylpropene + Methanol, + 1-Propanol, + 2-Propanol, + 2-Butanol, and + 2-Methyl-2-propanol Binary Systems at 364.5 K
• Solubility of Organic Systems Containing 1,4-Dioxan-2-one
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 9. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in Trimethyl-butylammonium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography and Static Method
• Vapor-Liquid Equilibria for the n-Pentane + 1-Propanol and n-Pentane + 2-Methyl-1-propanol Systems near the Critical Region
• Liquid-Liquid Equilibrium in Mixtures of the Ionic Liquid 1-n-Butyl-3-methylimidazolium Hexafluorophosphate and an Alkanol
• Temperature Effect on the Liquid-Liquid Equilibria for Some Aliphatic Alcohols + Water + K2CO3 Systems
• Vapor-Liquid Equilibrium Behaviors of Coumarin and Vanillin in Ethanol, 1-Propanol, and 2-Propanol
• Density and Surface Tension of Binary Mixtures of Acetonitrile + 1-Alkanol at 293.15 K
• Activity Coefficients at Infinite Dilution in 1-Alkyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
• 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
• Density and Viscosity of Binary Mixtures of Diethyl Carbonate with Alcohols at (293.15 to 363.15) K and Predictive Results by UNIFAC-VISCO Group Contribution Method
• Excess Molar Enthalpies of 1,2-Propanediol + Alkan-1-ols (C1-C6) and Their Correlations at 298.15 K and Ambient Pressure (81.5 kPa)
• Henry s Constants of 1-Alkanols and 2-Ketones in Salt Solutions
• Compressibility Studies of Binary Solutions Involving Water as a Solute in Nonaqueous Solvents at T ) 298.15 K
• Experimental Determination and Correlation of Phase Equilibria for the Ethane + 1-Propanol and Propane + 1-Propanol Systems
• Physical Properties of Binary Mixtures of the Ionic Liquid 1-Methyl-3-octylimidazolium Chloride with Methanol, Ethanol, and 1-Propanol at T = (298.15, 313.15, and 328.15) K and at P ) 0.1 MPa
• Measurement and Correlation of Solubilities of Luteolin in Organic Solvents at Different Temperatures
• Excess Molar Enthalpies, Molar Heat Capacities, Densities, Viscosities, and Refractive Indices of Dimethyl Sulfoxide + 1-Propanol at (288.15, 298.15, and 308.15) K and at Normal Pressure
• Measurement and Correlation of Vapor-Liquid Equilibria at T ) 333.15 K and Excess Molar Volumes at T ) 298.15 K for Ethanol + Dimethyl Carbonate (DMC), DMC + 1-Propanol, and DMC + 1-Butanol
• Liquid-Liquid Phase Equilibria of (1-Propanol or 2-Propanol + Water) Containing Dipotassium Hydrogen Phosphate
• Effect of Pressure on the Static Relative Permittivities of Alkan-1-ols at 298.15 K
• Phase Equilibrium Properties of Binary and Ternary Mixtures Containing 1,1-Dimethylethyl Methyl Ether, 1-Propanol, and Hexane at T ) 313.15 K
• Experimental Study of Thermodynamic Properties of Mixtures Containing Ionic Liquid 1-Ethyl-3-methylimidazolium Ethyl Sulfate Using Gas-Liquid Chromatography and Transpiration Method
• Activity Coefficients at Infinite Dilution of Polar Solutes in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Fluid-Phase Behavior of {1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Imide, [C6mim][NTf2], + C2-C8 n-Alcohol} Mixtures: Liquid-Liquid Equilibrium and Excess Volumes
• Isobaric Vapor-Liquid Equilibria for Binary and Ternary Mixtures of Dipropyl Ether, 1-Propyl Alcohol, and Butyl Propionate
• Vapor-Liquid Equilibria and HE for Binary Systems of Dimethyl Ether (DME) with C1-C4 Alkan-1-ols at 323.15 K and Liquid-Liquid Equilibria for Ternary System of DME + Methanol + Water at 313.15 K
• Phase Equilibria Involved in Extractive Distillation of Dipropyl Ether + 1-Propyl Alcohol Using N,N-Dimethylformamide as Entrainer
• Solubility of 1H-1,2,4-Triazole in Ethanol, 1-Propanol, 2-Propanol, 1,2-Propanediol, Ethyl Formate, Methyl Acetate, Ethyl Acetate, and Butyl Acetate at (283 to 363) K
• Densities and Excess Molar Volumes for Binary Glycerol + 1-Propanol, + 2-Propanol, + 1,2-Propanediol, and + 1,3-Propanediol Mixtures at Different Temperatures
• Solubility of Clopidogrel Hydrogen Sulfate (Form II) in Different Solvents
• Vapor-Liquid Equilibria for the Ternary System Acetonitrile + 1-Propanol + Dimethyl Sulfoxide and the Corresponding Binary Systems at 101.3 kPa
• Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Butyl-3-methyl-pyridinium Trifluoromethanesulfonate
• Excess Molar Enthalpies of Benzyl Alcohol + Alkanols (C1-C6) and Their Correlations at 298.15 K and Ambient Pressure
• Excess Molar Volumes of 1,3-Diethyl Propanedioate with Methanol, Ethanol, Propan-1-ol, Propan-2-ol, Butan-2-ol, 2-Methyl-propan-1-ol, and Pentan-1-ol at T = (288.15, 298.15, 313.15, and 328.15) K
• Solubility of Anthracene in C1-C3 Alcohols from (298.2 to 333.2) K and Their Mixtures with 2-Propanone at 298.2 K
• Solubilities of Ibuprofen in Different Pure Solvents
• Solubilities of Cefepime Hydrochloride in Water + (Ethanol, 1-Propanol, or 2-Propanol) from (278.15 to 308.15) K
• Solubility of 3,5-Dinitrobenzoic Acid in Supercritical Carbon Dioxide with Cosolvent at Temperatures from (308 to 328) K and Pressures from (10.0 to 21.0) MPa
• Solubilities of 2,4-Dinitro-l-phenylalanine in Monosolvents at (273.15 to 368.15) K
• Determination of Activity Coefficients at Infinite Dilution of 35 Solutes in the Ionic Liquid, 1-Butyl-3-methylimidazolium Tosylate, Using Gas-Liquid Chromatography
• Vapor Pressure Measurement and Correlation or Prediction for Water, 1-Propanol, 2-Propanol, and Their Binary Mixtures with [MMIM][DMP] Ionic Liquid
• Thermodynamic Parameters of Anionic Surfactant-Additive Systems at the Cloud Point
• Activity Coefficients at Infinite Dilution for Hydrocarbons in Fatty Alcohols Determined by Gas-Liquid Chromatography
• P, rho, T Measurements and Isobaric Vapor-Liquid-Equilibria of the 1,3,3-Trimethyl-2-oxabicycle[2,2,2]octane + Propan-1-ol Mixture: Cubic and Statistical Associating Fluid Theory-Based Equation of State Analysis
• PpT Measurements of the (Ethanol + Linalool), (Propan-1-ol + Linalool), and (Propan-2-ol + Linalool) Mixtures: Cubic and Statistical Associating Fluid Theory-Based Equation of State Analyses
• Excess Volume of the 1-Propanol + 1-Alkene Systems in Terms of an Equation of State with Association
• Solubility of Butyl Paraben in Methanol, Ethanol, Propanol, Ethyl Acetate, Acetone, and Acetonitrile
• Excess Molar Enthalpies of Methyl Acetoacetate + (Methanol, + Ethanol, + 1-Propanol, and + 2-Propanol) at T = (288.2, 298.2, 313.2, and 328.2) K and p = 101.3 kPa
• Solubility of Florfenicol in Different Solvents at Temperatures from (278 to 318) K
• Volumetric Properties for (Ionic Liquid + Methanol or Ethanol or 1-Propanol + Nitromethane) at 298.15 K and Atmospheric Pressure
• Densities and Viscosities of Binary Mixture of the Ionic Liquid Bis(2-hydroxyethyl)ammonium Propionate with Methanol, Ethanol, and 1-Propanol at T = (293.15, 303.15, 313.15, and 323.15) K and at P = 0.1 MPa
• Measurement and Correlation of Solubilities of Cefpirome Sulfate in Aqueous Alcohol Solution between (278.15 and 308.15) K
• Isobaric Vapor-Liquid Equilibria for Binary and Ternary Mixtures of Propanal, Propanol, and Propanoic Acid
• Solubility of Dimethyl Fumarate in Methanol, Ethanol, 1-Propanol, 2-Propanol, 1,2-Propanediol, and Water from (289.95 to 347.15) K
• Activity Coefficients at Infinite Dilution in Methylimidazolium Nitrate Ionic Liquids
• Solubility of Candesartan Cilexetil in Different Solvents at Various Temperatures
• Excess Molar Enthalpies of 2-Methyl-2-butanol (1) + 1-Alkanols (C1-C5) (2) at 298.15 K
• Measurement and Correlation for Solubility of 11alpha-Hydroxy-16alpha,17alpha-epoxyprogesterone and 16alpha,17alpha-Epoxyprogesterone in Solvents
• Solubility of Dexibuprofen in Different Solvents from (263.15 to 293.15) K
• Solubilities of Phloretin in 12 Solvents at Different Temperatures
• Densities and Viscosities of Binary Solutions of Benzene-1,3-diol + Water, Ethanol, Propan-1-ol, and Butan-1-ol at T = (293.15 to 333.15) K
• Measurement and Correlation of Solubilities of Asiaticoside in Water, Methanol, Ethanol, n-Propanol, n-Butanol, and a Methanol + Water Mixture from (278.15 to 343.15) K
• Solubilities of Pioglitazone Hydrochloride in Different Solvents
• Solubility of Minoxidil in Methanol, Ethanol, 1-Propanol, 2-Propanol, 1-Butanol, and Water from (278.15 to 333.15) K
• Phase Equilibria for Reactive Distillation of Propyl Propanoate. Pure Component Property Data, Vapor-Liquid Equilibria, and Liquid-Liquid Equilibria
• Solubility of CO2 in Alcohols, Glycols, Ethers, and Ketones at High Pressures from (288.15 to 318.15) K
• Densities and Viscosities of Four Binary Diethyl Carbonate + 1-Alcohol Systems from (288.15 to 313.15) K
• Measurement and Correlation of Solubilities of (Z)-2-(2-Aminothiazol-4-yl)-2-methoxyiminoacetic Acid in Different Pure Solvents and Binary Mixtures of Water + (Ethanol, Methanol, or Glycol)
• Phase Diagram Data for Ethanol/Propan-1-ol/Propan-2-ol-2,3-Dihydroxybutanedioate Aqueous Two-Phase Systems at 298.15 K and Data Correlation
• Measurement and Correlation for the Solubility of Dimethyl 1,4-Cyclohexanedione-2,5-dicarboxylate in Different Solvents at Temperatures from (278.15 to 323.15) K
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Butyl-3-methylimidazolium Nitrate Using Gas-Liquid Chromatography
• Measurement and Correlation of Solubility of Clopidogrel Hydrogen Sulfate (Metastable Form) in Lower Alcohols
• Solubility of 2-(2,4,6-Trichlorophenoxy)ethyl Bromide in Methanol, Ethanol, Propanol, Isopropanol, Acetonitrile, n-Heptane, and Acetone
• Activity Coefficients at Infinite Dilution of Organic Compounds in Four New Imidazolium-Based Ionic Liquids
• Liquid Liquid Phase Equilibria of 1-Propanol + Water + n-Alcohol Ternary Systems at 298.15 K and Atmospheric Pressure
• Isothermal Vapor Liquid Equilibrium Data of Propan-1-ol + 2,2,4-Trimethylpentane and Butan-1-ol + 2,2,4-Trimethylpentane at 318.15 K
• Isobaric Vapor Liquid Equilibria of 1-Propanol + Water + Trifluoromethanesulfonate-Based Ionic Liquid Ternary Systems at 100 kPa
• Measurement and Calculation of Liquid Liquid Equilibria of Ternary and Quaternary Systems Containing Water, Propan-1-ol, and 2,2,4-Trimethylpentane (TMP) with 2,2'-Oxybis(propane) (DIPE) or Dimethyl Carbonate (DMC)
• ACSExcess Molar Enthalpies of Mixtures of (+-)-Linalool with Several Alkanols
• Extraction of n-Alcohols from n-Heptane Using Ionic Liquids.
• Solubilities of Betulinic Acid in Thirteen Organic Solvents at Different Temperatures
• Activity Coefficients at Infinite Dilution by GLC in Alkanediamines as Stationary Phases
• Partition Coefficients of Organic Compounds in Four New Tetraalkylammonium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Using Inverse Gas Chromatography
• Density, Viscosity, and Refractive Index Properties for the Binary Mixtures of n-Butylammonium Acetate Ionic Liquid + Alkanols at Several Temperatures
• Interactions of Volatile Organic Compounds with the Ionic Liquid 1-Butyl-1-methylpyrrolidinium Dicyanamide
• Isobaric Vapor Liquid Equilibria for the 1-Propanol + Ethylene Glycol Monopropyl Ether and 1-Butanol + Ethylene Glycol Monopropyl Ether Systems
• Isothermal Vapor Liquid Equilibrium Data for the Propan-1-ol + Dodecane System at (323.0, 343.4, 353.2, 363.1, and 369.2) K
• Experimental Measurement and Modeling of Aniline Hydrochloride Solubility in Water, Methanol, Ethanol, 1- Propanol and Their Mixed Systems
• Densities and Viscosities for Binary Mixtures of the Ionic Liquid N-Ethyl Piperazinium Propionate with n-Alcohols at Several Temperatures
• Evaluation of the Performance of Trigeminal Tricationic Ionic Liquids for Separation Problems
• Excess Volumes of Ternary Mixtures 2,2,4-Trimethylpentane + Diisopropyl Ether or Methyl tert-Butyl Ether + Methanol, Ethanol, or 1-Propanol at 298.15 K
• Solubility and Solution Thermodynamics of Betaine in Different Pure Solvents and Binary Mixtures
• Densities and Viscosities of Naphthalen-1-ol, Naphthalen-2-ol, and 1-Aminonaphthalene in the Solvents of Ethanol, Propan-1-ol, and Butan-1-ol
• Binodal Curves and Tie-Lines of Aliphatic Alcohols + Diammonium Hydrogen Citrate + Water Ternary Systems: Measurement and Modeling
• Vapor Liquid Equilibrium Data for Binary Systems of 1-Methyl-4-(1-methylethenyl)-cyclohexene + {Ethanol, Propan-1-ol, Propan-2-ol, Butan-1-ol, Pentan-1-ol, or Hexan-1-ol} at 40 kPa
• Thermophysical Properties of the Pure Ionic Liquid 1-Butyl-1-methylpyrrolidinium Dicyanamide and Its Binary Mixtures with Alcohols
• Solubility of Vitamin D3 in Six Organic Solvents at Temperatures from (248.2 to 273.2) K
• Vapor Liquid Equilibrium Data for Binary Systems of 1H-Pyrrole with Butan-1-ol, Propan-1-ol, or Pentan-1-ol
• Determination and Correlation of Pyridazin-3-amine Solubility in Eight Organic Solvents at Temperatures Ranging from (288.05 to 333.35) K
• Liquid Liquid Equilibrium of Some Aliphatic Alcohols + Disodium Tartrate + Water Aqueous Two-Phase Systems at 298.15 K
• Isobaric Vapor Liquid Equilibria of Tertiary Amine and n-Alkane/Alkanol Binary Mixtures: Experimental Measurements and Modeling with GC-PPC-SAFT
• Densities and Viscosities for Binary Liquid Mixtures of Ethanol + 1-Propanol, 1-Butanol, and 1-Pentanol from (293.15 to 328.15) K at 0.1 MPa
• 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
• Isobaric Vapor Liquid Equilibrium Data of 2-Methyl-propan-2-ol (1) + Heptan-1-ol (2), Methanol (1) + Heptan-1-ol (2), Ethanol (1) + Heptan-1-ol (2), and Propan-1-ol (1) + Heptan-1-ol (2) at 96.5 kPa
• Solubility of N-Chloro-4-toluenesulfonamide Sodium and N-Chlorobenzenesulfonamide Sodium in Ethanol, Water, 1-Propanol, and Butan-2-ol
• Isobaric Vapor Liquid Equilibrium Data for Binary Mixtures of 1-Phenylethanone with a Few Alcohols at 95.2 kPa
• Vapor Pressures and Activity Coefficients of (1-Propanol + 1,8-Cineole) at 10 Temperatures between 278.15 K and 323.15 K
• Experimental Measurement and Modeling of Ternary Vapor Liquid Equilibrium for Water + 1-Propanol + 1-Butyl-3-methylimidazolium Chloride
• Vapor Liquid Liquid Equilibria Measurements for the Dehydration of Ethanol, Isopropanol, and n-Propanol via Azeotropic Distillation Using DIPE and Isooctane as Entrainers
• Solubility of 2-Hydroxybenzoic Acid in Water, 1-Propanol, 2-Propanol, and 2-Propanone at (298.2 to 338.2) K and Their Aqueous Binary Mixtures at 298.2 K
• Determination and Correlation of Solubility of Tris(3-hydroxypropyl)phosphine Oxide in Selected Solvents
• Density and Viscosity Measurements of Binary Alkanol Mixtures from (293.15 to 333.15) K at Atmospheric Pressure
• Measurement and Modeling of Vapor Liquid Equilibria for Systems Containing Alcohols, Water, and Imidazolium-Based Phosphate Ionic Liquids
• Liquid Liquid Equilibrium Data of the Ternary Systems Containing 1-Propanol/2-Propanol + Dipotassium Tartrate/Potassium Sodium Tartrate + Water at T = 298.15 K
• Solubility of Veratric Acid in Eight Monosolvents and Ethanol + 1-Butanol at Various Temperatures
• Determination and Correlation of Solubilities of (S)-Indoline-2-carboxylic Acid in Six Different Solvents from (283.15 to 358.15) K
• 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
• Determination and Correlation of Solubility of Cefradine Form I in Five Pure Solvents from (283.15 to 308.15) K
• Liquid Liquid Phase Behavior of Solutions of 1,3-Dimethylimidazolium- and 1-Methyl-3-propylimidazolium Bis((trifluoromethyl)sulphonyl)amide (C1,3mimNTf2) in n-Alkyl Alcohols
• Volumetric, Viscometric, and Refractive Index Behavior of 7-Hydroxy-4-methylcoumarin in Aqueous Ethanol or 1-Propanol Solutions in the Temperature Range of (293.15 to 313.15) K
• Volumetric and Transport Properties of Binary Mixtures of n-Octane + Ethanol, + 1-Propanol, + 1-Butanol, and + 1-Pentanol from (293.15 to 323.15) K at Atmospheric Pressure
• Composition and Temperature Dependence of Density, Surface Tension, and Viscosity of EMIM DEP/MMIM DMP + Water + 1-Propanol/2-Propanol Ternary Mixtures and Their Mathematical Representation Using the Jouyban Acree Model
• Experimental Determination of Vapor Liquid Equilibria. Binary Systems of Methyl Acetate, Ethyl Acetate, and Propyl Acetate with 1-Propanol at 0.6 MPa
• Solubility of Sodium Acetate in Binary Mixtures of Methanol, 1-Propanol, Acetonitrile, and Water at 298.2 K
• Measurement and Correlation of Solubility of 2-Chloro-4-ethylamino-6-isopropylamino-1,3,5-triazine in Different Organic Solvents
• Excess Molar Enthalpies of Binary Mixtures Containing 1-Methyl-3-octyl-imidazolium Tetrafluoroborate and Alcohols at T = 298.15 K
• Evaluation of the 2-Methoxyethanol as Entrainer in Ethanol Water and 1-Propanol Water Mixtures
• Measurement and Correlation of Solubilities of Indole-2-carboxylic Acid in Ten Different Pure Solvents from (278.15 to 360.15) K
• Densities and Viscosities of Diaminotoluene with Water, Ethanol, Propan-1-ol, and Butan-1-ol from (293.15 to 333.15) K
• Solubilities of 4-(Hydroxymethyl)-1-oxido-2,6,7-trioxa-1-phosphabicyclo[2.2.2]octane in Organic Solvents
• Thermodynamics of Fluconazole Solubility in Various Solvents at Different Temperatures
• Solubility of Dichloronitrobenzene in Eight Organic Solvents from T = (278.15 to 303.15) K: Measurement and Thermodynamic Modeling
• Measurement and Correlation of the Excess Properties of Ternary Mixture of {x1[Hmim][BF4] + x21-Propanol + x32-Propanol} at Different Temperatures
• Densities and Viscosities of Binary Mixtures Containing 1,3-Dimethylimidazolium Dimethylphosphate and Alcohols
• Measurement and Correlation of Solubility and Dissolution Thermodynamic Properties of Furan-2-carboxylic Acid in Pure and Binary Solvents
• Infinite Dilution Activity Coefficients of Solutes Dissolved in Two Trihexyl(tetradecyl)phosphonium Ionic Liquids
• Isobaric Vapor Liquid Liquid Equilibria for the Ternary Systems Ethanol + Water + Propyl Acetate and 1-Propanol + Water + Propyl acetate
• Determination and Correlation of Solubilities of Lauric Acid in Eight Alcohols
• Vapor Liquid Equilibrium Data for Binary Systems of n-Dodecane + {Propan-1-ol, Butan-1-ol, 2-Methylpropan-1-ol} at 40 kPa
• Oxygenated Compounds + Hydrocarbon Mixtures in Fuels and Biofuels: Excess Enthalpies of Ternary Mixtures Containing 1-Butoxybutane + Propan-1-ol +1-Hex-1-ene, or Heptane, or 2,2,4-Trimethylpentane at (298.15 and 313.15) K
• Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
• Solubility of Tris(hydroxymethyl)aminomethane in Water + 1-Propanol Mixtures at Various Temperatures
• Phase Equilibrium, Excess Enthalpies and Densities of Binary Mixtures of Trimethylbutylammonium Bis(trifluoromethylsulfonyl)imide with Ethanol, 1-Propanol and Dimethylformamide
• Speed of sound, density and related thermodynamic excess properties of binary mixtures of butan-2-one with C1-C4 nalkanols and chloroform
• Thermodynamic Properties of Polymorphs of 2,2'-Thiodiethylene Bis[3-(3,5-di-tert-butyl-4-hydroxyphenyl)propionate]
• Liquid Liquid Equilibria of Three Ternary Systems: {Glycerol + Benzene + Methanol}, {Glycerol + Benzene + Ethanol}, and {Glycerol + Benzene + 1-Propanol}
• Solubility of Tris(hydroxymethyl)aminomethane in Methanol + 1-Propanol Mixtures at Various Temperatures
• Densities and Viscosities of Binary Mixtures of 2,2,4-Trimethylpentane + 1-Propanol, + 1-Pentanol, + 1-Hexanol, and + 1-Heptanol from (298.15 to 323.15) K
• Determination and Modeling of the Solubility of 2,4-Dimethoxybenzoic Acid in Six Pure and Isopropanol + Ethyl Acetate Mixed Organic Solvents at Temperatures From (288.15 to 323.15) K
• Liquid Liquid Equilibrium for Ternary Systems Containing Water, Oleic Acid, and Alcohols at 313.15 K. Effect of Alcohol Chain Length
• Solubility of Anthracene in Binary Diisopropyl Ether + Alcohol Solvent Mixtures at 298.15 K
• Physical Properties of Binary Mixtures of the Ionic Liquid 1-Ethyl-3-methylimidazolium Ethyl Sulfate with Several Alcohols at T = (298.15, 313.15, and 328.15) K and Atmospheric Pressure
• Solubilities of Betulin in Fourteen Organic Solvents at Different Temperatures
• Isobaric Vapor-Liquid Equilibria for Three Ternary Systems: Water + 2-Propanol + 1-Ethyl-3-methylimidazolium Tetrafluoroborate, Water + 1-Propanol + 1-Ethyl-3-methylimidazolium Tetrafluoroborate, and Water + 1-Propanol + 1-Butyl-3-methylimidazolium Tetrafluoroborate
• Experimental Liquid-Liquid Equilibria of 1-Alkyl-3-methylimidazolium Hexafluorophosphate with 1-Alcohols
• Solubility of Chlorpheniramine Maleate in Ethanol, 1-Propanol, 1-Butanol, Benzene, Ethyl Acetate, Ethyl Formate, and Butyl Acetate between 283 K and 333 K
• Volumetric and Ultrasonic Studies of 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate Ionic Liquid with Methanol, Ethanol, 1-Propanol, and Water at Several Temperatures
• Solubility of 1-H-Tetrazole-1-acetic Acid in Different Solvents between 283 K and 323 K
• Solubility of Phenacetinum in Methanol, Ethanol, 1-Propanol, 1-Butanol, 1-Pentanol, Tetrahydrofuran, Ethyl Acetate, and Benzene between 282.65 K and 333.70 K
• Solid-Liquid Equilibria of Dibenzothiophene and Dibenzothiophene Sulfone in Organic Solvents
• Densities and Excess Molar Volumes of the Binary 1-Propanol + Chloroform and 1-Propanol + Benzene and Ternary 1-Propanol + Chloroform + Benzene Mixtures at (288.15, 293.15, 298.15, 303.15, 308.15, and 313.15) K
• Densities of Ionic Liquids, 1-Butyl-3-methylimidazolium Hexafluorophosphate and 1-Butyl-3-methylimidazolium Tetrafluoroborate, with Benzene, Acetonitrile, and 1-Propanol at T = (293.15 to 343.15) K
• Thermodynamic Properties of 1-Butyl-3-methylpyridinium Tetrafluoroborate and Its Mixtures with Water and Alkanols
• Solubilities of 2-Methyl-1,4-naphthoquinone in Water + (Methanol, Ethanol, 1-Propanol, 2-Propanol, 1,2-Propanediol, and Glycerin, Respectively) from (293.15 to 337.92) K
• Vapor-Liquid Equilibrium Behaviors of 3-Ethoxy-4-hydroxybenzaldehyde in Alcohol
• Solubility of 2-(4-Ethylbenzoyl)benzoic Acid in Eleven Organic Solvents between 279.55 K and 343.15 K
• Isothermal VLE and VE at 303.15 K for the Binary and Ternary Mixtures of Di-isopropyl Ether (DIPE) + 1-Propanol + 2,2,4-Trimethylpentane
• Excess Enthalpies of 2,4-Pentanedione + (Methanol, + Ethanol, + 1-Propanol, and + 2-Propanol) at T = (298.15, 313.15, and 328.15) K and p = (0.1 and 10.0) MPa
• Solubility of Trimethoprim (TMP) in Different Organic Solvents from (278 to 333) K
• Solubility of Anthracene in Binary Propyl Acetate + Alcohol Solvent Mixtures at 298.15 K
• Naphthalene Solubility in Binary Solvent Mixtures of 2,2,4-Trimethylpentane + Alcohols at 298.15 K
• Densities and Excess Molar Volumes of N-Methylmorpholine + 1-Alkanol Systems at 298.15 K
• Activity Coefficients at Infinite Dilution of Polar Solutes in 1-Butyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas Liquid Chromatography
• Liquid Liquid Equilibrium for Ternary Systems of Propyl Vinyl Ether + C3 or C4 Alcohols + Water at 298.15 K and Excess Molar Enthalpies for Ternary and Constituent Binary Systems of Propyl Vinyl Ether + Ethanol + Isooctane at 303.15 K
• Surface Tension and Density of Pure Ionic Liquids and Some Binary Mixtures with 1-Propanol and 1-Butanol
• Activity Coefficients at Infinite Dilution of Polar Solutes in 1-Propyl-2,3-dimethylimidazolium Tetrafluoroborate Using Gas Liquid Chromatography
• Excess Molar Enthalpies of Acetophenone + (Methanol, + Ethanol, + 1-Propanol, and + 2-Propanol) at Different Temperatures and Pressures
• Vapor Liquid Equilibrium for the Systems trans-2-Butene + Methanol, + 1-Propanol, + 2-Propanol, + 2-Butanol, and + 2-Methyl-2-propanol at 364.5 K
• Density and Viscosity Experimental Data of the Ternary Mixtures 1-Propanol or 2-Propanol + Water + 1-Ethyl-3-methylimidazolium Ethylsulfate. Correlation and Prediction of Physical Properties of the Ternary Systems
• Solubility of Losartan Potassium in Different Pure Solvents from (293.15 to 343.15) K
• Vapor Liquid Equilibrium Behaviors of 5-Methyl-2-(1-methylethyl)phenol in Alcohol
• Solubilities of Menadione Sodium Bisulfite in Water + (Methanol, Ethanol, 1-Propanol, 2-Propanol, 1,2-Propanediol, and Glycerin, Respectively) from (297.67 to 337.76) K
• 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
• Isobaric Vapor-Liquid Equilibria for Tetrahydropyran and Alcohol Systems
• Volumetric Properties of Binary and Ternary Liquid Mixtures of 1-Propanol (1) + 2-Propanol (2) + Water (3) at Different Temperatures and Ambient Pressure (81.5 kPa)
• Vapor-Liquid Equilibrium for 1-Butene + Methanol, + 1-Propanol, + 2-Propanol, + 2-Butanol, and 2-Methyl-2-propanol (TBA) at 364.5 K
• Solubility of Pravastatin Sodium in Water, Methanol, Ethanol, 2-Propanol, 1-Propanol, and 1-Butanol from (278 to 333) K
• Solubility of Carbamazepine (Form III) in Different Solvents from (275 to 343) K
• Measurement of Infinite Dilution Activity Coefficients of Alcohols, Ketones, and Aromatic Hydrocarbons in 4-Methyl-N-butylpyridinium Tetrafluoroborate and 1-Butyl-3-methylimidazolium Hexafluorophosphate by Gas-Liquid Chromatography
• Viscosities and Densities of Binary Mixtures of (N-Acetylmorpholine + Alkanols) from (293.15 to 323.15) K
• Solubility of 1-(2-Dimethylaminoethyl)-5-mercapto-1H-tetrazole in Water, DMF, Methanol, Ethanol, 1-Propanol, 2-Propanol, 1-Butanol, and 2-Butanol between (293 and 343) K
• Solubility of Alcohols and Aromatic Compounds in Imidazolium-Based Ionic Liquids
• Excess Molar Enthalpies of N,N-Dimethylethanolamine with (Methanol, Ethanol, 1-Propanol, and 2-Propanol) at T ) (298.2, 313.2, and 328.2) K and p ) (0.1 and 10.0) MPa
• Activity Coefficients at Infinite Dilution of Alkanols in the Ionic Liquids 1-Butyl-3-methylimidazolium Hexafluorophosphate, 1-Butyl-3-methylimidazolium Methyl Sulfate, and 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Amide Using the Dilutor Technique
• Isobaric Vapor-Liquid Equilibria for 1-Propanol + Water + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
• Binary Liquid-Liquid Equilibrium (LLE) for Dibutyl Ether (DBE) + Water from (288.15 to 318.15) K and Ternary LLE for Systems of DBE + C1 !less thanless than C4 Alcohols + Water at 298.15 K
• High-Pressure Phase Equilibria for the Carbon Dioxide + 1-Propanol System
• Densities and Kinematic Viscosities of Ten Binary 1-Alkanol Liquid Systems at Temperatures of (293.15 and 298.15) K
• Solubility of D(-)-p-Hydroxyphenylglycine Dane Salt in Eight Alcohols between (293 and 343) K
• Solubility of Benzoic Acid in Aqueous Solutions Containing Ethanol or N-Propanol
• Measurement and Correlation of the Solubilities of m-Phthalic Acid in Monobasic Alcohols
• Ternary Liquid-Liquid Equilibria for Systems Containing Alcohol or Acetic Acid + Ester + 1-Ethyl-3-methylimidazolium Hydrogen Sulfate at 313.2 K Using Headspace Gas Chromatography
• Solubility of Sebacic Acid in Binary Mixtures Containing Alcohols
• Solubility of Diphenyl Carbonate in Pure Alcohols from (283 to 333) K
• Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Inverse Gas Chromatography
• Solubility of Salol in Pure Alcohols from (283.15 to 308.15) K
• Binary Liquid-Liquid Equilibrium (LLE) for Methyl tert-Amyl Ether (TAME) + Water from (288.15 to 313.15) K and Ternary LLE for Systems of TAME + C1-C4 Alcohols + Water at 298.15 K
• Density, Viscosity, and Electrical Conductivity in the Potassium Sulfate + Water + 1-Propanol System at Different Temperatures
• Solubility of Fluorene in Benzene, Chloroform, Acetone, 1-Propanol, Isobutanol, and Methylbenzene from (283 to 323) K
• Solubility of Acenaphthene in Different Solvents from (283.00 to 323.00) K
• Solubility of Indinavir Sulfate in Different Solvents from (278.35 to 314.15) K
• Solubilities of Lauric Acid in n-Hexane, Acetone, Propanol, 2-Propanol, 1-Bromopropane, and Trichloroethylene from (279.0 to 315.3) K
• Activity Coefficients at Infinite Dilution of Organic Compounds in Trihexyl(tetradecyl)phosphonium Bis(trifluoromethylsulfonyl)imide Using Inverse Gas Chromatography
• Excess Molar Enthalpies of Ternary and Binary Mixtures Containing 2-Methoxy-2-methylpropane, 1-Propanol, and Nonane
• Solubilities of Isonicotinic Acid in (Methanol, Ethanol, 1-Propanol, 2-Propanol, and 1,2-Propanediol, Respectively) from (289.65 to 358.75) K
• Temperature and Composition Dependence of the Density and Viscosity of Binary Mixtures of {1-Butyl-3-methylimidazolium Thiocyanate + 1-Alcohols}
• Densities and Excess Molar Volumes of Cyclopentane (1) + 1-Alkanol (2) Systems at (298.15 and 308.15) K
• Paramagnetic Ionic Liquid 1-Butyl-3-methylimidazolium Tetrabromidocobaltate(II): Activity Coefficients at Infinite Dilution of Organic Solutes and Crystal Structure
• Densities and Viscosities of Binary Mixtures of Cyclopropanecarboxylic Acid with Methanol, Ethanol, Propan-1-ol, and Butan-1-ol at Different Temperatures
• Binary and Ternary Vapor-Liquid Equilibrium at 323.15 K and Excess Molar Volumes at 298.15 K for the Mixtures of Propyl Vinyl Ether + 1-Propanol + Toluene
• Experimental Determination, Correlation, and Prediction of Physical Properties of the Ternary Mixtures Ethanol and 1-Propanol + Water + 1-Ethyl-3-methylpyridinium Ethylsulfate at 298.15 K
• Synthesis and Physical Properties of 1-Ethylpyridinium Ethylsulfate and its Binary Mixtures with Ethanol and 1-Propanol at Several Temperatures
• Solubility of Butanedioic Acid in Different Solvents at Temperatures between 283 K and 333 K
• Solubility of Phenanthrene in Binary Mixtures of C1-C4 Alcohols + 2-Propanol and Ethanol + Methanol at 298.15 K
• Solubility of p-Aminobenzenesulfonamide in Different Solvents from (283.15 to 323.15) K
• Solubility and Liquid-Liquid Equilibrium of Aqueous Systems of Iodoethane with Methanol, Ethanol, or 1-Propanol at Temperature 298.15 K and Pressure 101.2 kPa
• Solubility of Fumaric Acid in Propan-2-ol, Ethanol, Acetone, Propan-1-ol, and Water
• Solubility of Thiotriazinone in Ethanol, 1-Propanol, 2-Propanol, 1-Butanol, Acetonitrile, Acetone, Ethyl Acetate, and Water from 293 K to 343 K
• Densities and Viscosities of (1-Propanol + 1,2-Dichloroethane), (1-Propanol + Benzaldehyde), (Benzaldehyde + 1,2-Dichloroethane), and (1-Propanol + 1,2-Dichloroethane + Benzaldehyde) Mixtures from T = 288.15 K to 313.15 K
• Dynamic Viscosity of the Binary System 1-Propanol + Toluene as a Function of Temperature and Pressure
• Isobaric Vapor-Liquid Equilibria at 101.32 kPa and Densities, Speeds of Sound, and Refractive Indices at 298.15 K for MTBE or DIPE or TAME + 1-Propanol Binary Systems
• Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
• Liquid-Liquid Equilibria, Density, Viscosity, and Surface and Interfacial Tension of the System Water + n-Butyl Acetate + 1-Propanol at 323.15 K and Atmospheric Pressure
• Excess Molar Enthalpies of Diethyl Malonate + (Methanol, + Ethanol, + 1-Propanol, and + 2-Propanol) at T = (288.2, 298.2, 313.2, and 328.2) K and p = 101.3 kPa
• Apparent Molal Volumes and Viscosity B-Coefficients of Acetyl Salicylic Acid (2-Acetoxy Benzoic Acid) Solutions in Higher Alcohols at Different Temperatures
• Phase Diagrams of Ammonium Sulfate + Ethanol/1-Propanol/2-Propanol + Water Aqueous Two-Phase Systems at 298.15 K and Correlation
• Solubility of Phenanthrene in Binary Mixtures of C1-C4 Alcohols at 298.2 K
• Refractive Indices and Deviations in Refractive Indices for Binary Mixtures of 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate with Methanol, Ethanol, 1-Propanol, and 2-Propanol at Several Temperatures
• Solubility and Density of Potassium Iodide in a Binary Propan-1-ol-Water Solvent Mixture at (298.15, 303.15, 308.15, and 313.15) K
• Solubility of Vitamin C in Water, Ethanol, Propan-1-ol, Water + Ethanol, and Water + Propan-1-ol at (298.15 and 308.15) K
• Activity Coefficients at Infinite Dilution of Polar Solutes in 1-(2-Hydroxyethyl)-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Solubilities of Sulfadiazine in Methanol, Ethanol, 1-Propanol, 2-Propanol, Acetone, and Chloroform from (294.15 to 318.15) K
• Solubility of N-(Phosphonomethyl)iminodiacetic Acid in Different Binary Mixtures
• Solubility of Avermectin B1a in Some Pure and Mixed Solvents from (278.2 to 318.2) K
• Solubilities of (?,Z)-2-Amino-?-(methoxyimino)-4-thiazole-ethanethioic Acid S-2-Benzothiazolyl Ester in Pure Solvents and a Mixture of Acetonitrile and Dichloromethane
• Liquid-Liquid Equilibria for Aliphatic Alcohols + Dipotassium Oxalate + Water
• 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
• Apparent Molar Volume and Compressibility of Tetrabutylphosphonium Bromide in Various Solvents
• Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Hexyl-3-methylimidazolium Thiocyanate
• Molar Volumes and Refractive Indexes of Hexane-1,2,3,4,5,6-hexol in Aqueous Solutions of 1-Propanol and 2-Propanol
• Solubility of Glyphosate in Ethanol + Water, 1-Propanol + Water, and 2-Propanol + Water from (293 to 333) K
• Densities and Viscosities of Pure 1-Methyl-3-octylimidazolium Nitrate and Its Binary Mixtures with Alcohols at Several Temperatures
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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