Chemical Properties of 1-Butanol (CAS 71-36-3)

InChI

InChI=1S/C4H10O/c1-2-3-4-5/h5H,2-4H2,1H3

InChI Key

LRHPLDYGYMQRHN-UHFFFAOYSA-N

Formula

C4H10O

SMILES

CCCCO

Molecular Weight¹

74.12

CAS

71-36-3

Other Names

• 1-Butyl alcohol
• 1-Hydroxybutane
• Alcool butylique
• Butan-1-ol
• Butanol
• Butanol-1
• Butanolen
• Butanolo
• Butyl alcohol
• Butyl hydroxide
• Butylowy alkohol
• Butyric alcohol
• CCS 203
• Hemostyp
• METHYLOLPROPANE
• N-BUTYL ALCOHOL
• NSC 62782
• Propylcarbinol
• Propylmethanol
• Rcra waste number U031
• n-Butan-1-ol
• n-Butanol
• n-C4H9OH

• 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).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• σ_cond : Electrical conductivity (S/m).
• 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).
• ν : Kinematic viscosity (m²/s).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_c : Critical density (kg/m³).
• ρ_g : Gas Density (kg/m³).
• 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).
• 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).
• 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	0.5930		KDB
PAff	789.20	kJ/mol	NIST
Tig	616.48	K	KDB
BasG	758.90	kJ/mol	NIST
ΔcH°liquid	[-2677.40; -2640.00]	kJ/mol
ΔcH°liquid	-2676.18 ± 0.24	kJ/mol	NIST
ΔcH°liquid	Outlier -2640.00 ± 120.00	kJ/mol	NIST
ΔcH°liquid	-2675.61 ± 0.45	kJ/mol	NIST
ΔcH°liquid	-2676.01 ± 0.24	kJ/mol	NIST
ΔcH°liquid	-2677.40 ± 0.63	kJ/mol	NIST
ΔcH°liquid	-2674.90 ± 0.84	kJ/mol	NIST
ΔcH°liquid	-2670.40 ± 0.42	kJ/mol	NIST
ΔcH°liquid	-2670.44	kJ/mol	NIST
ΔcH°liquid	-2676.00	kJ/mol	NIST
ΔcH°liquid	-2670.77	kJ/mol	NIST
μ	1.80	debye	KDB
η	[0.0025383; 0.0025730]	Pa×s
η	0.0025730	Pa×s	Study o...
η	0.0025650	Pa×s	Thermod...
η	0.0025383	Pa×s	Densiti...
LFL	1.40	% in Air	KDB
UFL	11.20	% in Air	KDB
Tflash,cc	309.26	K	KDB
Tflash,oc	302.04	K	KDB
ΔfG°	-150.90	kJ/mol	KDB
Rg	3.2250		KDB
ΔfH°gas	[-281.40; -273.50]	kJ/mol
ΔfH°gas	-274.90	kJ/mol	KDB
ΔfH°gas	-275.60	kJ/mol	NIST
ΔfH°gas	-274.70 ± 0.30	kJ/mol	NIST
ΔfH°gas	-275.28 ± 0.53	kJ/mol	NIST
ΔfH°gas	-275.80	kJ/mol	NIST
ΔfH°gas	-274.90 ± 0.30	kJ/mol	NIST
ΔfH°gas	-274.40	kJ/mol	NIST
ΔfH°gas	-273.50 ± 0.70	kJ/mol	NIST
ΔfH°gas	-280.00 ± 0.92	kJ/mol	NIST
ΔfH°gas	-277.00 ± 1.50	kJ/mol	NIST
ΔfH°gas	-281.40	kJ/mol	NIST
ΔfH°gas	-280.50 ± 0.40	kJ/mol	NIST
ΔfH°gas	-278.20	kJ/mol	NIST
ΔfH°gas	-277.30 ± 3.00	kJ/mol	NIST
ΔfH°liquid	[-332.80; -325.80]	kJ/mol
ΔfH°liquid	-327.01 ± 0.24	kJ/mol	NIST
ΔfH°liquid	-327.58 ± 0.52	kJ/mol	NIST
ΔfH°liquid	-327.18 ± 0.24	kJ/mol	NIST
ΔfH°liquid	-325.80 ± 0.67	kJ/mol	NIST
ΔfH°liquid	-328.40 ± 0.84	kJ/mol	NIST
ΔfH°liquid	Outlier -332.80 ± 0.42	kJ/mol	NIST
ΔfH°liquid	-329.60	kJ/mol	NIST
ΔfusH°	10.20	kJ/mol	Joback Calculated Property
ΔvapH°	41.18	kJ/mol	Joback Calculated Property
IE	[9.99; 10.64]	eV
IE	9.99 ± 0.05	eV	NIST
IE	10.10 ± 0.05	eV	NIST
IE	9.99 ± 0.05	eV	NIST
IE	10.64 ± 0.07	eV	NIST
IE	10.09 ± 0.02	eV	NIST
IE	10.37	eV	NIST
IE	10.37	eV	NIST
IE	10.04	eV	NIST
IE	10.43	eV	NIST
IE	10.44 ± 0.03	eV	NIST
IE	10.37	eV	NIST
log10WS	[0.00; 0.00]
log10WS	0.00		Aq. Sol...
log10WS	0.00		Estimat...
logPoct/wat	0.779		Crippen Calculated Property
McVol	73.090	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
NFPA Health	1		KDB
Pc	[4410.00; 4924.00]	kPa
Pc	4414.00	kPa	KDB
Pc	4410.00 ± 20.00	kPa	NIST
Pc	4410.00	kPa	NIST
Pc	4418.00 ± 20.00	kPa	NIST
Pc	4418.00 ± 20.00	kPa	NIST
Pc	4423.00	kPa	NIST
Pc	4413.00	kPa	NIST
Pc	4413.00	kPa	NIST
Pc	4415.00	kPa	NIST
Pc	Outlier 4924.00 ± 30.00	kPa	NIST
Pc	Outlier 4904.13 ± 60.79	kPa	NIST
ρc	[266.84; 274.99]	kg/m3
ρc	271.29 ± 1.48	kg/m3	NIST
ρc	269.80	kg/m3	NIST
ρc	271.29 ± 2.96	kg/m3	NIST
ρc	274.99	kg/m3	NIST
ρc	269.88	kg/m3	NIST
ρc	266.84	kg/m3	NIST
ρc	270.02 ± 2.22	kg/m3	NIST
Inp	[618.00; 692.00]
Inp	674.40		NIST
Inp	674.60		NIST
Inp	668.20		NIST
Inp	665.50		NIST
Inp	658.40		NIST
Inp	653.10		NIST
Inp	648.20		NIST
Inp	642.00		NIST
Inp	645.00		NIST
Inp	653.30		NIST
Inp	653.30		NIST
Inp	650.00		NIST
Inp	648.90		NIST
Inp	647.70		NIST
Inp	647.60		NIST
Inp	661.90		NIST
Inp	659.20		NIST
Inp	657.30		NIST
Inp	650.00		NIST
Inp	648.90		NIST
Inp	647.70		NIST
Inp	647.60		NIST
Inp	661.90		NIST
Inp	659.20		NIST
Inp	657.30		NIST
Inp	636.00		NIST
Inp	646.00		NIST
Inp	646.80		NIST
Inp	643.90		NIST
Inp	661.90		NIST
Inp	659.60		NIST
Inp	663.00		NIST
Inp	675.00		NIST
Inp	663.00		NIST
Inp	645.00		NIST
Inp	651.00		NIST
Inp	649.00		NIST
Inp	649.00		NIST
Inp	660.00		NIST
Inp	647.00		NIST
Inp	650.00		NIST
Inp	645.00		NIST
Inp	637.00		NIST
Inp	645.00		NIST
Inp	649.90		NIST
Inp	636.00		NIST
Inp	Outlier 620.00		NIST
Inp	Outlier 619.00		NIST
Inp	Outlier 618.00		NIST
Inp	642.00		NIST
Inp	644.00		NIST
Inp	645.00		NIST
Inp	630.00		NIST
Inp	650.00		NIST
Inp	643.00		NIST
Inp	643.00		NIST
Inp	644.00		NIST
Inp	627.00		NIST
Inp	673.00		NIST
Inp	637.00		NIST
Inp	Outlier 625.00		NIST
Inp	655.00		NIST
Inp	651.00		NIST
Inp	654.00		NIST
Inp	657.00		NIST
Inp	654.00		NIST
Inp	654.00		NIST
Inp	671.00		NIST
Inp	647.00		NIST
Inp	649.00		NIST
Inp	649.00		NIST
Inp	676.00		NIST
Inp	663.00		NIST
Inp	664.00		NIST
Inp	652.00		NIST
Inp	655.00		NIST
Inp	646.00		NIST
Inp	665.00		NIST
Inp	667.00		NIST
Inp	650.05		NIST
Inp	658.70		NIST
Inp	Outlier 680.00		NIST
Inp	Outlier 686.00		NIST
Inp	Outlier 688.00		NIST
Inp	Outlier 690.00		NIST
Inp	662.00		NIST
Inp	661.00		NIST
Inp	660.00		NIST
Inp	662.00		NIST
Inp	659.00		NIST
Inp	668.00		NIST
Inp	653.00		NIST
Inp	668.00		NIST
Inp	651.00		NIST
Inp	669.00		NIST
Inp	660.10		NIST
Inp	661.50		NIST
Inp	Outlier 621.00		NIST
Inp	668.00		NIST
Inp	654.50		NIST
Inp	Outlier 619.00		NIST
Inp	Outlier 619.00		NIST
Inp	653.00		NIST
Inp	660.00		NIST
Inp	659.00		NIST
Inp	659.00		NIST
Inp	658.00		NIST
Inp	653.00		NIST
Inp	Outlier 619.00		NIST
Inp	Outlier 619.00		NIST
Inp	647.10		NIST
Inp	647.10		NIST
Inp	645.00		NIST
Inp	649.60		NIST
Inp	673.20		NIST
Inp	653.00		NIST
Inp	659.00		NIST
Inp	646.00		NIST
Inp	640.00		NIST
Inp	666.00		NIST
Inp	664.00		NIST
Inp	669.00		NIST
Inp	647.00		NIST
Inp	659.00		NIST
Inp	659.00		NIST
Inp	641.00		NIST
Inp	645.00		NIST
Inp	643.00		NIST
Inp	640.00		NIST
Inp	640.00		NIST
Inp	642.00		NIST
Inp	641.00		NIST
Inp	641.00		NIST
Inp	649.00		NIST
Inp	641.00		NIST
Inp	639.00		NIST
Inp	638.00		NIST
Inp	643.00		NIST
Inp	650.00		NIST
Inp	648.00		NIST
Inp	664.00		NIST
Inp	Outlier 692.00		NIST
Inp	650.00		NIST
Inp	654.00		NIST
Inp	655.00		NIST
Inp	650.00		NIST
Inp	656.00		NIST
Inp	670.00		NIST
Inp	664.00		NIST
Inp	664.00		NIST
Inp	664.00		NIST
Inp	646.00		NIST
Inp	668.00		NIST
Inp	Outlier 688.00		NIST
Inp	670.00		NIST
Inp	665.00		NIST
Inp	668.00		NIST
Inp	643.00		NIST
Inp	643.00		NIST
Inp	635.00		NIST
Inp	642.48		NIST
Inp	663.00		NIST
Inp	652.00		NIST
Inp	638.00		NIST
Inp	655.00		NIST
Inp	Outlier 681.00		NIST
Inp	653.00		NIST
Inp	633.00		NIST
Inp	634.00		NIST
Inp	633.00		NIST
Inp	634.00		NIST
Inp	661.00		NIST
Inp	656.00		NIST
Inp	655.00		NIST
Inp	647.00		NIST
Inp	655.00		NIST
Inp	637.00		NIST
Inp	640.00		NIST
Inp	640.00		NIST
Inp	657.00		NIST
Inp	661.00		NIST
Inp	654.00		NIST
Inp	670.00		NIST
Inp	657.00		NIST
Inp	Outlier 684.00		NIST
Inp	653.00		NIST
Inp	666.00		NIST
Inp	653.00		NIST
Inp	639.00		NIST
Inp	663.00		NIST
Inp	650.00		NIST
Inp	646.00		NIST
Inp	655.00		NIST
Inp	658.00		NIST
Inp	650.00		NIST
Inp	653.00		NIST
Inp	653.00		NIST
Inp	668.00		NIST
Inp	657.00		NIST
Inp	650.00		NIST
Inp	655.00		NIST
Inp	654.00		NIST
Inp	653.00		NIST
Inp	646.00		NIST
Inp	653.00		NIST
Inp	653.00		NIST
Inp	Outlier 680.00		NIST
Inp	635.00		NIST
Inp	632.00		NIST
Inp	646.00		NIST
Inp	650.00		NIST
Inp	652.00		NIST
Inp	656.00		NIST
Inp	656.00		NIST
Inp	650.00		NIST
Inp	651.00		NIST
Inp	638.00		NIST
Inp	659.00		NIST
Inp	655.00		NIST
Inp	655.00		NIST
Inp	661.00		NIST
Inp	646.00		NIST
Inp	651.00		NIST
Inp	646.00		NIST
Inp	Outlier 680.00		NIST
Inp	641.00		NIST
Inp	642.00		NIST
Inp	639.00		NIST
Inp	664.00		NIST
I	[1094.00; 1181.00]
I	1120.00		NIST
I	1147.50		NIST
I	1146.00		NIST
I	Outlier 1178.00		NIST
I	1126.00		NIST
I	Outlier 1104.00		NIST
I	1148.00		NIST
I	1124.00		NIST
I	1153.00		NIST
I	1131.00		NIST
I	1133.33		NIST
I	1130.99		NIST
I	1129.04		NIST
I	1135.08		NIST
I	1135.00		NIST
I	Outlier 1178.00		NIST
I	1120.00		NIST
I	1118.00		NIST
I	1152.00		NIST
I	1137.00		NIST
I	1115.00		NIST
I	1136.00		NIST
I	1138.00		NIST
I	1152.00		NIST
I	1143.00		NIST
I	1135.00		NIST
I	1160.00		NIST
I	1148.00		NIST
I	1113.00		NIST
I	1150.00		NIST
I	1150.00		NIST
I	1164.00		NIST
I	1175.00		NIST
I	1160.00		NIST
I	1113.00		NIST
I	1128.00		NIST
I	1153.00		NIST
I	1157.00		NIST
I	1125.00		NIST
I	1145.90		NIST
I	1145.00		NIST
I	1150.00		NIST
I	1125.00		NIST
I	1146.00		NIST
I	1154.00		NIST
I	1147.00		NIST
I	1116.00		NIST
I	1134.00		NIST
I	1137.00		NIST
I	1132.00		NIST
I	1154.00		NIST
I	1161.00		NIST
I	1164.00		NIST
I	1165.00		NIST
I	1116.00		NIST
I	1140.00		NIST
I	1147.00		NIST
I	1166.00		NIST
I	1125.00		NIST
I	1159.70		NIST
I	1132.00		NIST
I	1126.00		NIST
I	1144.00		NIST
I	1126.00		NIST
I	1144.00		NIST
I	1172.00		NIST
I	1128.00		NIST
I	1126.00		NIST
I	1144.00		NIST
I	1172.00		NIST
I	1130.00		NIST
I	1144.00		NIST
I	1145.00		NIST
I	Outlier 1179.00		NIST
I	1126.00		NIST
I	1110.00		NIST
I	1136.00		NIST
I	1150.00		NIST
I	1149.00		NIST
I	1141.00		NIST
I	1115.00		NIST
I	1141.00		NIST
I	1136.00		NIST
I	1136.00		NIST
I	1141.00		NIST
I	1113.00		NIST
I	1115.00		NIST
I	1136.00		NIST
I	1163.00		NIST
I	1136.00		NIST
I	1140.00		NIST
I	1124.00		NIST
I	1148.00		NIST
I	1156.00		NIST
I	1131.00		NIST
I	1119.00		NIST
I	1126.00		NIST
I	1152.00		NIST
I	1153.00		NIST
I	1155.00		NIST
I	1136.00		NIST
I	1149.00		NIST
I	1119.00		NIST
I	1119.00		NIST
I	1118.00		NIST
I	1136.00		NIST
I	1119.00		NIST
I	1152.00		NIST
I	1155.00		NIST
I	1149.00		NIST
I	1149.00		NIST
I	1142.00		NIST
I	1120.00		NIST
I	1132.00		NIST
I	1173.00		NIST
I	1151.00		NIST
I	1119.00		NIST
I	1119.00		NIST
I	1136.00		NIST
I	1142.00		NIST
I	1142.00		NIST
I	1139.00		NIST
I	1136.00		NIST
I	1147.00		NIST
I	1145.00		NIST
I	Outlier 1180.00		NIST
I	Outlier 1094.00		NIST
I	1122.00		NIST
I	1161.00		NIST
I	1162.00		NIST
I	1164.00		NIST
I	1148.00		NIST
I	1163.00		NIST
I	Outlier 1104.00		NIST
I	1173.00		NIST
I	1152.00		NIST
I	1147.00		NIST
I	1132.00		NIST
I	1147.00		NIST
I	1137.00		NIST
I	1113.00		NIST
I	1137.00		NIST
I	1137.00		NIST
I	1143.00		NIST
I	1165.00		NIST
I	1159.00		NIST
I	1156.00		NIST
I	1167.00		NIST
I	1113.00		NIST
I	1132.00		NIST
I	1133.00		NIST
I	1136.00		NIST
I	1139.00		NIST
I	1147.00		NIST
I	1133.00		NIST
I	1147.00		NIST
I	1138.00		NIST
I	1138.00		NIST
I	Outlier 1180.00		NIST
I	1132.00		NIST
I	1145.00		NIST
I	1138.00		NIST
I	1135.00		NIST
I	1164.00		NIST
I	1161.00		NIST
I	1162.00		NIST
I	1146.00		NIST
I	1148.00		NIST
I	1140.00		NIST
I	1136.00		NIST
I	1138.00		NIST
I	Outlier 1103.00		NIST
I	1129.00		NIST
I	1138.00		NIST
I	1148.00		NIST
I	1135.00		NIST
I	1111.00		NIST
I	1176.00		NIST
I	1163.00		NIST
I	1115.00		NIST
I	1113.00		NIST
I	1115.00		NIST
I	1147.00		NIST
I	1143.00		NIST
I	1113.00		NIST
I	1151.00		NIST
I	1140.00		NIST
I	1143.00		NIST
I	1138.00		NIST
I	1142.00		NIST
I	1140.00		NIST
I	1132.00		NIST
I	1156.00		NIST
I	1140.00		NIST
I	1113.00		NIST
I	1118.00		NIST
I	1118.00		NIST
I	1121.00		NIST
I	1113.00		NIST
I	1145.00		NIST
I	1137.00		NIST
I	1113.00		NIST
I	1113.00		NIST
I	1113.00		NIST
I	1113.00		NIST
I	1113.00		NIST
I	1123.00		NIST
I	1139.00		NIST
I	1145.00		NIST
I	1148.00		NIST
I	1149.00		NIST
I	1159.00		NIST
I	1158.00		NIST
I	1153.00		NIST
I	1153.00		NIST
I	1152.00		NIST
I	1163.00		NIST
I	1159.00		NIST
I	1142.00		NIST
I	1119.00		NIST
I	1135.00		NIST
I	1135.00		NIST
I	1166.00		NIST
I	1158.00		NIST
I	1147.00		NIST
I	1124.00		NIST
I	1165.00		NIST
I	1166.00		NIST
I	1166.00		NIST
I	1152.00		NIST
I	1165.00		NIST
I	1152.00		NIST
I	1153.00		NIST
I	1159.00		NIST
I	1144.00		NIST
I	1165.00		NIST
I	1144.00		NIST
I	1116.00		NIST
I	1143.00		NIST
I	1145.00		NIST
I	1134.00		NIST
I	1144.00		NIST
I	1135.00		NIST
I	1110.00		NIST
I	1149.00		NIST
I	1144.00		NIST
I	1144.00		NIST
I	Outlier 1181.00		NIST
I	1141.00		NIST
I	1144.00		NIST
I	1157.00		NIST
I	1136.00		NIST
I	1155.00		NIST
I	1155.00		NIST
I	1139.00		NIST
I	1148.00		NIST
I	1113.00		NIST
I	1148.00		NIST
I	1148.00		NIST
I	1148.00		NIST
I	1163.00		NIST
I	1163.00		NIST
I	1151.00		NIST
I	1113.00		NIST
I	1141.00		NIST
I	1125.00		NIST
I	1148.00		NIST
I	1148.00		NIST
I	1135.00		NIST
I	1141.00		NIST
I	1139.00		NIST
I	1113.00		NIST
I	Outlier 1178.00		NIST
I	1128.00		NIST
I	1161.00		NIST
I	Outlier 1104.00		NIST
I	1147.00		NIST
I	1143.00		NIST
I	1113.00		NIST
I	Outlier 1180.00		NIST
I	1164.00		NIST
I	1140.00		NIST
I	1138.00		NIST
I	1163.00		NIST
I	1120.00		NIST
I	1133.33		NIST
I	Outlier 1178.00		NIST
I	1115.00		NIST
I	1135.00		NIST
I	1142.00		NIST
I	1145.00		NIST
I	1153.00		NIST
I	1158.00		NIST
I	1166.00		NIST
I	1159.00		NIST
I	1110.00		NIST
I	1141.00		NIST
I	1155.00		NIST
I	1148.00		NIST
I	1128.00		NIST
S°gas	361.98	J/mol×K	NIST
S°liquid	[225.73; 251.90]	J/mol×K
S°liquid	225.73	J/mol×K	NIST
S°liquid	228.00	J/mol×K	NIST
S°liquid	251.90	J/mol×K	NIST
Tboil	[355.70; 450.74]	K
Tboil	390.88	K	KDB
Tboil	390.83	K	Experim...
Tboil	390.75	K	Excess ...
Tboil	390.12	K	Vapor l...
Tboil	390.85	K	Measure...
Tboil	390.12	K	Liquid ...
Tboil	390.65	K	Isobari...
Tboil	390.82	K	Isobari...
Tboil	390.80	K	Solubil...
Tboil	390.84	K	Isobari...
Tboil	390.40	K	Isother...
Tboil	390.82	K	Isobari...
Tboil	390.79	K	Isobari...
Tboil	390.78	K	Isobari...
Tboil	390.83	K	Measure...
Tboil	390.75	K	Vapor-L...
Tboil	390.91	K	Isobari...
Tboil	390.86	K	Measure...
Tboil	390.65	K	Vapor L...
Tboil	390.48	K	Phase E...
Tboil	390.49	K	Vapor L...
Tboil	390.85	K	Vapor-L...
Tboil	390.85	K	Vapor-L...
Tboil	390.81	K	Vapor L...
Tboil	390.95	K	Isobari...
Tboil	390.77 ± 0.07	K	NIST
Tboil	390.70 ± 0.40	K	NIST
Tboil	390.80 ± 0.10	K	NIST
Tboil	390.80 ± 0.25	K	NIST
Tboil	390.75 ± 0.40	K	NIST
Tboil	390.40	K	NIST
Tboil	391.00	K	NIST
Tboil	390.85 ± 0.25	K	NIST
Tboil	390.92 ± 0.10	K	NIST
Tboil	390.75 ± 0.30	K	NIST
Tboil	390.90	K	NIST
Tboil	390.85 ± 0.40	K	NIST
Tboil	390.85 ± 0.30	K	NIST
Tboil	Outlier 450.74 ± 0.10	K	NIST
Tboil	390.15 ± 0.40	K	NIST
Tboil	389.85 ± 0.40	K	NIST
Tboil	390.80 ± 0.40	K	NIST
Tboil	390.10 ± 0.50	K	NIST
Tboil	390.65 ± 0.30	K	NIST
Tboil	390.55 ± 0.08	K	NIST
Tboil	390.80 ± 0.40	K	NIST
Tboil	390.80 ± 0.30	K	NIST
Tboil	390.80 ± 0.30	K	NIST
Tboil	391.20 ± 0.30	K	NIST
Tboil	390.51 ± 0.20	K	NIST
Tboil	390.90 ± 0.30	K	NIST
Tboil	390.75 ± 0.30	K	NIST
Tboil	391.00 ± 0.40	K	NIST
Tboil	390.35 ± 0.30	K	NIST
Tboil	390.90 ± 0.30	K	NIST
Tboil	390.85	K	NIST
Tboil	390.75 ± 0.30	K	NIST
Tboil	391.00 ± 0.15	K	NIST
Tboil	390.80 ± 0.50	K	NIST
Tboil	390.20 ± 2.00	K	NIST
Tboil	390.87 ± 0.50	K	NIST
Tboil	390.85 ± 0.30	K	NIST
Tboil	390.85 ± 0.40	K	NIST
Tboil	390.85 ± 0.30	K	NIST
Tboil	390.67 ± 0.20	K	NIST
Tboil	390.95 ± 0.20	K	NIST
Tboil	390.85 ± 0.40	K	NIST
Tboil	389.15 ± 2.00	K	NIST
Tboil	390.85	K	NIST
Tboil	390.15 ± 0.50	K	NIST
Tboil	390.85 ± 0.50	K	NIST
Tboil	390.50 ± 0.50	K	NIST
Tboil	390.95 ± 0.30	K	NIST
Tboil	389.30 ± 1.00	K	NIST
Tboil	390.85 ± 0.50	K	NIST
Tboil	390.65 ± 1.00	K	NIST
Tboil	390.65 ± 0.30	K	NIST
Tboil	390.15 ± 1.00	K	NIST
Tboil	390.95 ± 0.50	K	NIST
Tboil	390.65 ± 0.30	K	NIST
Tboil	390.85 ± 0.50	K	NIST
Tboil	390.65 ± 0.50	K	NIST
Tboil	390.25 ± 0.30	K	NIST
Tboil	390.85 ± 0.50	K	NIST
Tboil	390.75 ± 0.20	K	NIST
Tboil	390.15 ± 0.50	K	NIST
Tboil	388.15 ± 2.00	K	NIST
Tboil	390.56 ± 0.20	K	NIST
Tboil	389.90 ± 1.00	K	NIST
Tboil	390.85 ± 0.30	K	NIST
Tboil	390.50 ± 0.50	K	NIST
Tboil	391.15 ± 1.00	K	NIST
Tboil	390.55 ± 0.30	K	NIST
Tboil	389.65 ± 1.00	K	NIST
Tboil	391.05 ± 0.50	K	NIST
Tboil	390.80 ± 0.50	K	NIST
Tboil	390.95 ± 0.50	K	NIST
Tboil	389.65 ± 1.00	K	NIST
Tboil	389.90 ± 1.00	K	NIST
Tboil	390.55 ± 0.05	K	NIST
Tboil	390.85 ± 0.30	K	NIST
Tboil	391.25 ± 0.50	K	NIST
Tboil	390.95 ± 0.30	K	NIST
Tboil	391.00 ± 0.40	K	NIST
Tboil	390.95 ± 0.50	K	NIST
Tboil	390.80 ± 0.50	K	NIST
Tboil	390.00 ± 1.00	K	NIST
Tboil	390.82 ± 0.25	K	NIST
Tboil	390.95 ± 0.30	K	NIST
Tboil	390.75 ± 0.30	K	NIST
Tboil	391.15 ± 1.00	K	NIST
Tboil	390.65 ± 1.00	K	NIST
Tboil	390.95 ± 0.30	K	NIST
Tboil	390.85 ± 0.50	K	NIST
Tboil	390.15 ± 1.00	K	NIST
Tboil	390.85 ± 0.50	K	NIST
Tboil	390.75 ± 0.50	K	NIST
Tboil	390.85 ± 0.50	K	NIST
Tboil	388.90 ± 2.00	K	NIST
Tboil	390.15 ± 1.00	K	NIST
Tboil	390.87 ± 0.05	K	NIST
Tboil	390.85 ± 0.50	K	NIST
Tboil	391.15 ± 0.50	K	NIST
Tboil	390.00 ± 3.00	K	NIST
Tboil	389.65 ± 1.00	K	NIST
Tboil	391.15 ± 1.00	K	NIST
Tboil	390.86 ± 0.10	K	NIST
Tboil	390.40 ± 0.10	K	NIST
Tboil	390.84 ± 0.10	K	NIST
Tboil	390.50 ± 0.50	K	NIST
Tboil	390.55 ± 0.50	K	NIST
Tboil	390.57 ± 0.20	K	NIST
Tboil	390.90 ± 0.30	K	NIST
Tboil	390.90 ± 0.25	K	NIST
Tboil	390.30 ± 0.30	K	NIST
Tboil	390.45 ± 0.50	K	NIST
Tboil	390.40 ± 0.50	K	NIST
Tboil	390.90 ± 0.40	K	NIST
Tboil	391.15 ± 0.20	K	NIST
Tboil	390.75 ± 0.30	K	NIST
Tboil	Outlier 355.70 ± 0.50	K	NIST
Tboil	390.65 ± 0.50	K	NIST
Tboil	390.80 ± 0.50	K	NIST
Tboil	389.40 ± 1.00	K	NIST
Tboil	390.90 ± 0.20	K	NIST
Tboil	390.95 ± 0.20	K	NIST
Tboil	389.75 ± 0.50	K	NIST
Tboil	390.70 ± 0.70	K	NIST
Tboil	391.00 ± 0.30	K	NIST
Tboil	390.60 ± 0.50	K	NIST
Tboil	390.00 ± 1.50	K	NIST
Tboil	390.65 ± 0.50	K	NIST
Tboil	390.85 ± 0.50	K	NIST
Tboil	390.80 ± 0.50	K	NIST
Tboil	390.25 ± 0.20	K	NIST
Tboil	390.65 ± 0.30	K	NIST
Tboil	390.75 ± 0.30	K	NIST
Tboil	389.55 ± 0.70	K	NIST
Tboil	390.86 ± 0.05	K	NIST
Tboil	390.75 ± 0.50	K	NIST
Tboil	390.25 ± 0.20	K	NIST
Tboil	389.65 ± 1.00	K	NIST
Tboil	390.90 ± 0.50	K	NIST
Tboil	390.65 ± 0.30	K	NIST
Tboil	389.65 ± 0.50	K	NIST
Tboil	389.15 ± 2.00	K	NIST
Tboil	390.17 ± 0.20	K	NIST
Tboil	390.65 ± 0.50	K	NIST
Tboil	390.00 ± 1.50	K	NIST
Tboil	390.03 ± 1.50	K	NIST
Tboil	389.65 ± 2.50	K	NIST
Tboil	380.15 ± 2.00	K	NIST
Tc	[560.10; 564.20]	K
Tc	563.00	K	KDB
Tc	563.00	K	Measure...
Tc	563.00 ± 0.30	K	NIST
Tc	563.60	K	NIST
Tc	562.40 ± 0.60	K	NIST
Tc	562.40 ± 0.60	K	NIST
Tc	562.40	K	NIST
Tc	562.90	K	NIST
Tc	562.20 ± 0.20	K	NIST
Tc	562.20 ± 0.30	K	NIST
Tc	562.20 ± 0.30	K	NIST
Tc	562.20 ± 0.40	K	NIST
Tc	562.20 ± 0.40	K	NIST
Tc	561.00 ± 2.00	K	NIST
Tc	563.05	K	NIST
Tc	563.01	K	NIST
Tc	560.20	K	NIST
Tc	564.20	K	NIST
Tc	560.20	K	NIST
Tc	562.92	K	NIST
Tc	560.10 ± 0.20	K	NIST
Tc	561.20	K	NIST
Tc	560.30	K	NIST
Tfus	[183.30; 193.65]	K
Tfus	183.30	K	KDB
Tfus	183.63	K	Aq. Sol...
Tfus	183.70	K	Phase e...
Tfus	183.85	K	NIST
Tfus	183.85	K	NIST
Tfus	193.15 ± 5.00	K	NIST
Tfus	192.55 ± 0.50	K	NIST
Tfus	184.00 ± 2.00	K	NIST
Tfus	193.65 ± 1.00	K	NIST
Tfus	183.35 ± 0.20	K	NIST
Ttriple	[183.90; 184.54]	K
Ttriple	184.51	K	KDB
Ttriple	184.54 ± 0.02	K	NIST
Ttriple	184.51 ± 0.05	K	NIST
Ttriple	183.90 ± 0.20	K	NIST
Vc	[0.274; 0.274]	m3/kmol
Vc	0.274	m3/kmol	KDB
Vc	0.274	m3/kmol	NIST
Zc	0.2583670		KDB
Zra	0.25		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[137.88; 189.31]	J/mol×K	[395.25; 603.35]
T(K) Ideal gas heat capacity (J/mol×K) 140 150 160 170 180 190 400 500 600
Cp,gas	140.93 ± 0.79	J/mol×K	395.25	NIST
Cp,gas	137.88	J/mol×K	398.15	NIST
Cp,gas	143.00 ± 0.79	J/mol×K	404.15	NIST
Cp,gas	144.16 ± 0.79	J/mol×K	409.15	NIST
Cp,gas	142.06	J/mol×K	413.15	NIST
Cp,gas	146.58 ± 0.79	J/mol×K	419.55	NIST
Cp,gas	149.26 ± 0.79	J/mol×K	431.05	NIST
Cp,gas	147.42	J/mol×K	433.15	NIST
Cp,gas	151.60 ± 0.79	J/mol×K	441.15	NIST
Cp,gas	152.66	J/mol×K	453.15	NIST
Cp,gas	155.88 ± 0.79	J/mol×K	459.55	NIST
Cp,gas	162.55 ± 0.79	J/mol×K	488.25	NIST
Cp,gas	169.95 ± 0.79	J/mol×K	520.05	NIST
Cp,gas	175.97 ± 0.79	J/mol×K	545.95	NIST
Cp,gas	181.20 ± 0.79	J/mol×K	568.45	NIST
Cp,gas	189.31 ± 0.79	J/mol×K	603.35	NIST
Cp,liquid	[168.00; 222.54]	J/mol×K	[283.15; 353.15]
T(K) Liquid phase heat capacity (J/mol×K) 170 180 190 200 210 220 300 320 340
Cp,liquid	168.00	J/mol×K	283.15	Isobari...
Cp,liquid	171.00	J/mol×K	288.15	Isobari...
Cp,liquid	174.10	J/mol×K	293.15	Isobari...
Cp,liquid	173.80	J/mol×K	293.15	Molar h...
Cp,liquid	174.30	J/mol×K	293.15	NIST
Cp,liquid	175.30	J/mol×K	294.00	NIST
Cp,liquid	183.30	J/mol×K	298.00	NIST
Cp,liquid	174.50	J/mol×K	298.00	NIST
Cp,liquid	177.70	J/mol×K	298.00	NIST
Cp,liquid	176.67	J/mol×K	298.15	NIST
Cp,liquid	177.18	J/mol×K	298.15	NIST
Cp,liquid	175.97	J/mol×K	298.15	NIST
Cp,liquid	176.86	J/mol×K	298.15	NIST
Cp,liquid	176.69	J/mol×K	298.15	NIST
Cp,liquid	177.03	J/mol×K	298.15	NIST
Cp,liquid	177.10	J/mol×K	298.15	Molar h...
Cp,liquid	177.90	J/mol×K	298.15	Isobari...
Cp,liquid	177.08	J/mol×K	298.15	NIST
Cp,liquid	179.50	J/mol×K	301.20	NIST
Cp,liquid	215.50	J/mol×K	302.60	NIST
Cp,liquid	180.30	J/mol×K	303.00	NIST
Cp,liquid	180.61	J/mol×K	303.15	Molar h...
Cp,liquid	181.10	J/mol×K	303.15	Isobari...
Cp,liquid	181.60	J/mol×K	303.50	NIST
Cp,liquid	184.50	J/mol×K	308.15	Isobari...
Cp,liquid	184.28	J/mol×K	308.15	Molar h...
Cp,liquid	188.02	J/mol×K	313.15	Molar h...
Cp,liquid	187.80	J/mol×K	313.15	Isobari...
Cp,liquid	191.40	J/mol×K	318.15	Isobari...
Cp,liquid	192.10	J/mol×K	318.15	Molar h...
Cp,liquid	192.20	J/mol×K	321.05	NIST
Cp,liquid	189.10	J/mol×K	323.00	NIST
Cp,liquid	196.13	J/mol×K	323.15	Molar h...
Cp,liquid	196.00	J/mol×K	323.15	Isobari...
Cp,liquid	200.40	J/mol×K	328.15	Molar h...
Cp,liquid	200.10	J/mol×K	328.15	Isobari...
Cp,liquid	204.10	J/mol×K	333.15	Isobari...
Cp,liquid	204.72	J/mol×K	333.15	Molar h...
Cp,liquid	209.16	J/mol×K	338.15	Molar h...
Cp,liquid	208.40	J/mol×K	338.15	Isobari...
Cp,liquid	213.57	J/mol×K	343.15	Molar h...
Cp,liquid	218.10	J/mol×K	348.15	Molar h...
Cp,liquid	222.54	J/mol×K	353.15	Molar h...
η	[0.0006300; 0.0038794]	Pa×s	[283.15; 363.15]
T(K) Dynamic viscosity (Pa×s) 5.00e-4 1.00e-3 1.50e-3 2.00e-3 2.50e-3 3.00e-3 3.50e-3 4.00e-3 300 320 340 360
η	0.0038690	Pa×s	283.15	Excess ...
η	0.0038690	Pa×s	283.15	Excess ...
η	0.0038220	Pa×s	283.15	Density...
η	0.0038794	Pa×s	283.15	Density...
η	0.0033748	Pa×s	288.15	Densiti...
η	0.0033911	Pa×s	288.15	Density...
η	0.0033460	Pa×s	288.15	Densiti...
η	0.0032860	Pa×s	288.15	Densiti...
η	0.0033460	Pa×s	288.15	Densiti...
η	0.0029630	Pa×s	293.15	Density...
η	0.0029290	Pa×s	293.15	Densiti...
η	0.0028590	Pa×s	293.15	Density...
η	0.0029410	Pa×s	293.15	Densiti...
η	0.0029446	Pa×s	293.15	Densiti...
η	0.0029410	Pa×s	293.15	Dynamic...
η	0.0029410	Pa×s	293.15	Viscosi...
η	0.0029380	Pa×s	293.15	Viscosi...
η	0.0029590	Pa×s	293.15	Viscosi...
η	0.0029420	Pa×s	293.15	Viscosi...
η	0.0030100	Pa×s	293.15	Density...
η	0.0029410	Pa×s	293.15	Propert...
η	0.0029356	Pa×s	293.15	Molecul...
η	0.0029401	Pa×s	293.15	Densiti...
η	0.0029530	Pa×s	293.15	Density...
η	0.0025612	Pa×s	298.15	Densiti...
η	0.0026190	Pa×s	298.15	Density...
η	0.0025609	Pa×s	298.15	Excess ...
η	0.0025720	Pa×s	298.15	Densiti...
η	0.0026062	Pa×s	298.15	Density...
η	0.0025730	Pa×s	298.15	Propert...
η	0.0025710	Pa×s	298.15	Dynamic...
η	0.0025580	Pa×s	298.15	Density...
η	0.0025850	Pa×s	298.15	Densiti...
η	0.0025660	Pa×s	298.15	Densiti...
η	0.0025660	Pa×s	298.15	Density...
η	0.0025809	Pa×s	298.15	Densiti...
η	0.0025880	Pa×s	298.15	Densiti...
η	0.0025600	Pa×s	298.15	Densiti...
η	0.0025416	Pa×s	298.15	Molecul...
η	0.0025768	Pa×s	298.15	Densiti...
η	0.0025640	Pa×s	298.15	Viscosi...
η	0.0025609	Pa×s	298.15	Excess ...
η	0.0025730	Pa×s	298.15	Tempera...
η	0.0026180	Pa×s	298.15	Excess ...
η	0.0025720	Pa×s	298.15	Viscosi...
η	0.0025600	Pa×s	298.15	Densiti...
η	0.0025710	Pa×s	298.15	Viscosi...
η	0.0022550	Pa×s	303.15	Dynamic...
η	0.0022719	Pa×s	303.15	Densiti...
η	0.0022750	Pa×s	303.15	Tempera...
η	0.0022970	Pa×s	303.15	Excess ...
η	0.0022710	Pa×s	303.15	Viscosi...
η	0.0022751	Pa×s	303.15	Molecul...
η	0.0022630	Pa×s	303.15	Density...
η	0.0022962	Pa×s	303.15	Densiti...
η	0.0022820	Pa×s	303.15	Viscosi...
η	0.0022750	Pa×s	303.15	Viscosi...
η	0.0022550	Pa×s	303.15	Viscosi...
η	0.0022360	Pa×s	303.15	Density...
η	0.0022740	Pa×s	303.15	Densiti...
η	0.0023147	Pa×s	303.15	Density...
η	0.0022719	Pa×s	303.15	Densiti...
η	0.0022650	Pa×s	303.15	Density...
η	0.0022980	Pa×s	303.15	Density...
η	0.0022866	Pa×s	303.15	Densiti...
η	0.0022640	Pa×s	303.15	Propert...
η	0.0022750	Pa×s	303.15	Densiti...
η	0.0022600	Pa×s	303.15	Densiti...
η	0.0020020	Pa×s	308.15	Propert...
η	0.0020655	Pa×s	308.15	Density...
η	0.0019980	Pa×s	308.15	Density...
η	0.0019910	Pa×s	308.15	Densiti...
η	0.0020081	Pa×s	308.15	Densiti...
η	0.0020120	Pa×s	308.15	Densiti...
η	0.0019910	Pa×s	308.15	Densiti...
η	0.0020000	Pa×s	308.15	Viscosi...
η	0.0019073	Pa×s	308.15	Viscosi...
η	0.0020253	Pa×s	308.15	Densiti...
η	0.0019978	Pa×s	308.15	Molecul...
η	0.0019980	Pa×s	308.15	Densiti...
η	0.0019810	Pa×s	308.15	Tempera...
η	0.0018947	Pa×s	308.15	Viscosi...
η	0.0019910	Pa×s	308.15	Densiti...
η	0.0020320	Pa×s	308.15	Excess ...
η	0.0020104	Pa×s	308.15	Densiti...
η	0.0017820	Pa×s	313.15	Densiti...
η	0.0017567	Pa×s	313.15	Excess ...
η	0.0017690	Pa×s	313.15	Densiti...
η	0.0016813	Pa×s	313.15	Viscosi...
η	0.0017954	Pa×s	313.15	Densiti...
η	0.0017567	Pa×s	313.15	Excess ...
η	0.0017856	Pa×s	313.15	Densiti...
η	0.0017690	Pa×s	313.15	Density...
η	0.0017442	Pa×s	313.15	Molecul...
η	0.0017940	Pa×s	313.15	Viscosi...
η	0.0017673	Pa×s	313.15	Densiti...
η	0.0018476	Pa×s	313.15	Density...
η	0.0016840	Pa×s	313.15	Viscosi...
η	0.0017860	Pa×s	313.15	Density...
η	0.0017780	Pa×s	313.15	Density...
η	0.0017830	Pa×s	313.15	Densiti...
η	0.0017880	Pa×s	313.15	Propert...
η	0.0017360	Pa×s	313.15	Density...
η	0.0015690	Pa×s	318.15	Densiti...
η	0.0015872	Pa×s	318.15	Densiti...
η	0.0015712	Pa×s	318.15	Molecul...
η	0.0015500	Pa×s	318.15	Densiti...
η	0.0015690	Pa×s	318.15	Densiti...
η	0.0015953	Pa×s	318.15	Densiti...
η	0.0016597	Pa×s	318.15	Density...
η	0.0015550	Pa×s	318.15	Densiti...
η	0.0014188	Pa×s	323.15	Densiti...
η	0.0010980	Pa×s	323.15	Viscosi...
η	0.0014170	Pa×s	323.15	Densiti...
η	0.0014140	Pa×s	323.15	Densiti...
η	0.0014210	Pa×s	323.15	Density...
η	0.0014060	Pa×s	323.15	Thermop...
η	0.0014952	Pa×s	323.15	Density...
η	0.0012714	Pa×s	328.15	Densiti...
η	0.0013567	Pa×s	328.15	Density...
η	0.0012280	Pa×s	328.15	Densiti...
η	0.0012435	Pa×s	333.15	Density...
η	0.0011543	Pa×s	333.15	Viscosi...
η	0.0011340	Pa×s	333.15	Thermop...
η	0.0011430	Pa×s	333.15	Densiti...
η	0.0011370	Pa×s	333.15	Density...
η	0.0011381	Pa×s	333.15	Densiti...
η	0.0009810	Pa×s	338.15	Densiti...
η	0.0010275	Pa×s	338.15	Densiti...
η	0.0009306	Pa×s	343.15	Densiti...
η	0.0009200	Pa×s	343.15	Density...
η	0.0007590	Pa×s	353.15	Density...
η	0.0007837	Pa×s	353.15	Viscosi...
η	0.0006300	Pa×s	363.15	Density...
σcond	[4.40e-05; 8.00e-05]	S/m	[298.15; 318.15]
T(K) Electrical conductivity (S/m) 4.50e-5 5.00e-5 5.50e-5 6.00e-5 6.50e-5 7.00e-5 7.50e-5 8.00e-5 300 305 310 315
σcond	4.40e-05	S/m	298.15	Electri...
σcond	5.55e-05	S/m	303.15	Electri...
σcond	6.58e-05	S/m	308.15	Electri...
σcond	6.90e-05	S/m	313.15	Electri...
σcond	8.00e-05	S/m	318.15	Electri...
ΔfusH	[9.28; 9.37]	kJ/mol	[183.90; 184.50]
ΔfusH	9.28	kJ/mol	183.90	NIST
ΔfusH	9.28	kJ/mol	183.90	NIST
ΔfusH	9.28	kJ/mol	183.90	NIST
ΔfusH	9.37	kJ/mol	184.50	NIST
ΔvapH	[20.80; 55.00]	kJ/mol	[230.00; 530.00]
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 20 25 30 35 40 45 50 55 300 400 500
ΔvapH	51.60	kJ/mol	230.00	NIST
ΔvapH	49.50 ± 0.10	kJ/mol	333.00	NIST
ΔvapH	53.00	kJ/mol	343.00	NIST
ΔvapH	48.60 ± 0.10	kJ/mol	343.00	NIST
ΔvapH	55.00	kJ/mol	346.00	NIST
ΔvapH	48.30	kJ/mol	352.00	NIST
ΔvapH	49.90	kJ/mol	352.50	NIST
ΔvapH	47.50 ± 0.10	kJ/mol	353.00	NIST
ΔvapH	47.20 ± 0.10	kJ/mol	356.00	NIST
ΔvapH	49.00	kJ/mol	360.00	NIST
ΔvapH	46.40 ± 0.10	kJ/mol	363.00	NIST
ΔvapH	48.30	kJ/mol	363.50	NIST
ΔvapH	50.10	kJ/mol	368.00	NIST
ΔvapH	46.00	kJ/mol	373.00	NIST
ΔvapH	47.20	kJ/mol	374.00	NIST
ΔvapH	46.60	kJ/mol	380.00	NIST
ΔvapH	45.40 ± 0.10	kJ/mol	381.00	NIST
ΔvapH	45.30	kJ/mol	383.50	NIST
ΔvapH	45.40	kJ/mol	386.50	NIST
ΔvapH	45.30	kJ/mol	387.50	NIST
ΔvapH	43.09	kJ/mol	390.60	KDB
ΔvapH	43.29	kJ/mol	390.90	NIST
ΔvapH	43.10 ± 0.10	kJ/mol	391.00	NIST
ΔvapH	43.80	kJ/mol	410.00	NIST
ΔvapH	38.20	kJ/mol	423.00	NIST
ΔvapH	41.90	kJ/mol	458.00	NIST
ΔvapH	29.60	kJ/mol	473.00	NIST
ΔvapH	41.90	kJ/mol	481.50	NIST
ΔvapH	42.10	kJ/mol	491.00	NIST
ΔvapH	20.80	kJ/mol	523.00	NIST
ΔvapH	37.40	kJ/mol	530.00	NIST
ν	[0.0000022; 0.0000032]	m2/s	[298.15; 313.15]
ν	0.0000032	m2/s	298.15	Viscosi...
ν	0.0000022	m2/s	313.15	Viscosi...
Pvap	[0.20; 2027.00]	kPa	[278.15; 513.15]
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 300 400 500
Pvap	0.20	kPa	278.15	Isother...
Pvap	0.31	kPa	283.15	Isother...
Pvap	0.45	kPa	288.15	Isother...
Pvap	0.56	kPa	293.15	Dibutyl...
Pvap	0.66	kPa	293.15	Isother...
Pvap	0.94	kPa	298.15	Isother...
Pvap	0.91	kPa	298.15	(Vapour...
Pvap	1.00	kPa	298.15	Vapor-P...
Pvap	0.84	kPa	298.15	Dibutyl...
Pvap	1.09	kPa	301.02	Thermog...
Pvap	1.32	kPa	303.15	Vapor-P...
Pvap	1.32	kPa	303.15	Isother...
Pvap	1.23	kPa	303.15	Dibutyl...
Pvap	1.46	kPa	305.59	Thermog...
Pvap	1.83	kPa	308.15	Isother...
Pvap	1.79	kPa	308.15	(Vapour...
Pvap	1.76	kPa	308.15	Dibutyl...
Pvap	1.84	kPa	308.15	Vapor-P...
Pvap	1.92	kPa	310.16	Thermog...
Pvap	1.96	kPa	310.26	Thermog...
Pvap	1.91	kPa	310.29	Thermog...
Pvap	1.90	kPa	310.29	Thermog...
Pvap	2.54	kPa	313.15	Vapor-P...
Pvap	2.51	kPa	313.15	Isother...
Pvap	2.53	kPa	313.15	Isother...
Pvap	2.44	kPa	313.15	Dibutyl...
Pvap	2.48	kPa	313.15	Vapour-...
Pvap	2.70	kPa	314.19	Vapor-L...
Pvap	2.67	kPa	314.75	Thermog...
Pvap	2.60	kPa	314.76	Thermog...
Pvap	2.50	kPa	314.76	Thermog...
Pvap	2.61	kPa	314.81	Thermog...
Pvap	3.45	kPa	318.15	Vapor-P...
Pvap	3.33	kPa	318.15	Dibutyl...
Pvap	3.44	kPa	318.15	Isother...
Pvap	3.60	kPa	318.35	Vapor-L...
Pvap	3.90	kPa	318.35	Vapor-L...
Pvap	3.60	kPa	318.40	Vapor-L...
Pvap	4.15	kPa	321.34	Thermog...
Pvap	4.19	kPa	321.34	Thermog...
Pvap	4.33	kPa	322.07	Thermog...
Pvap	4.48	kPa	322.58	Thermog...
Pvap	4.52	kPa	322.69	Thermog...
Pvap	4.54	kPa	323.09	Thermog...
Pvap	4.54	kPa	323.14	Thermog...
Pvap	4.65	kPa	323.15	Vapor-P...
Pvap	4.61	kPa	323.15	Vapor-L...
Pvap	4.35	kPa	323.15	Dibutyl...
Pvap	4.54	kPa	323.15	Isother...
Pvap	4.49	kPa	323.20	Vapor-L...
Pvap	4.62	kPa	323.50	Thermog...
Pvap	4.69	kPa	323.67	Thermog...
Pvap	4.75	kPa	323.78	Thermog...
Pvap	4.74	kPa	323.90	Thermog...
Pvap	4.79	kPa	324.18	Thermog...
Pvap	4.85	kPa	324.28	Thermog...
Pvap	4.91	kPa	324.57	Thermog...
Pvap	4.87	kPa	324.59	Thermog...
Pvap	4.95	kPa	324.80	Thermog...
Pvap	4.98	kPa	324.91	Thermog...
Pvap	6.17	kPa	328.15	Vapor-P...
Pvap	5.33	kPa	328.15	Dibutyl...
Pvap	8.39	kPa	333.15	Vapor L...
Pvap	8.10	kPa	333.15	Vapor-P...
Pvap	8.09	kPa	333.51	Thermog...
Pvap	8.38	kPa	334.32	Thermog...
Pvap	10.56	kPa	338.15	Vapor-P...
Pvap	10.38	kPa	338.21	Vapor-L...
Pvap	12.79	kPa	341.78	Thermog...
Pvap	12.89	kPa	342.17	Vapor-L...
Pvap	13.60	kPa	343.15	Vapor-P...
Pvap	13.52	kPa	343.20	Thermog...
Pvap	13.71	kPa	343.36	Thermog...
Pvap	14.44	kPa	343.39	Thermog...
Pvap	17.37	kPa	348.15	Vapor-P...
Pvap	21.03	kPa	352.70	Thermog...
Pvap	21.44	kPa	352.81	Vapor-L...
Pvap	21.98	kPa	353.15	Vapor-P...
Pvap	25.30	kPa	356.35	Isobari...
Pvap	27.65	kPa	358.15	Vapor-P...
Pvap	29.30	kPa	359.45	Isobari...
Pvap	32.09	kPa	360.58	Thermog...
Pvap	31.52	kPa	361.24	Vapor-L...
Pvap	33.50	kPa	362.95	Isobari...
Pvap	34.41	kPa	363.15	Vapor-P...
Pvap	34.47	kPa	363.20	(Vapour...
Pvap	36.90	kPa	364.50	Vapour ...
Pvap	36.30	kPa	364.52	Vapor-L...
Pvap	40.00	kPa	366.76	Isobari...
Pvap	42.80	kPa	368.60	Isobari...
Pvap	49.26	kPa	371.94	Vapor-L...
Pvap	52.50	kPa	373.45	Isobari...
Pvap	53.33	kPa	373.74	Isobari...
Pvap	60.00	kPa	376.78	Isobari...
Pvap	61.20	kPa	377.30	Isobari...
Pvap	66.66	kPa	379.43	Isobari...
Pvap	72.80	kPa	381.90	Isobari...
Pvap	79.99	kPa	384.26	Isobari...
Pvap	80.00	kPa	384.28	Isobari...
Pvap	85.00	kPa	385.75	Experim...
Pvap	84.90	kPa	386.05	Isobari...
Pvap	93.32	kPa	388.49	Isobari...
Pvap	98.66	kPa	390.04	Isobari...
Pvap	100.00	kPa	390.28	Isobari...
Pvap	101.30	kPa	390.48	Phase E...
Pvap	101.30	kPa	390.49	Vapor L...
Pvap	101.30	kPa	390.65	Vapor L...
Pvap	101.30	kPa	390.65	Isobari...
Pvap	101.47	kPa	390.69	Vapor-L...
Pvap	101.30	kPa	390.75	Vapor-L...
Pvap	105.30	kPa	391.95	Isobari...
Pvap	110.26	kPa	393.15	Vapor L...
Pvap	120.10	kPa	395.80	Isobari...
Pvap	127.02	kPa	397.19	Vapor-L...
Pvap	152.42	kPa	402.79	Vapor-L...
Pvap	177.83	kPa	407.58	Vapor-L...
Pvap	203.23	kPa	411.88	Vapor-L...
Pvap	228.64	kPa	415.88	Vapor-L...
Pvap	833.00	kPa	468.15	Isother...
Pvap	1182.00	kPa	483.15	Isother...
Pvap	1558.00	kPa	498.15	Isother...
Pvap	2027.00	kPa	513.15	Isother...
n0	[1.38688; 1.40135]		[288.15; 323.15]
T(K) Refractive Index 1.39 1.4 1.4 290 300 310 320
n0	1.40100		288.15	Excess ...
n0	1.40135		288.15	Experim...
n0	1.40135		288.15	Experim...
n0	1.40130		288.20	Experim...
n0	1.39928		293.15	Ternary...
n0	1.39940		293.15	Liquid ...
n0	1.39890		293.15	Isother...
n0	1.39860		293.15	Solid-L...
n0	1.39970		293.15	Measure...
n0	1.39940		293.15	Refract...
n0	1.39932		293.15	Experim...
n0	1.39930		293.15	Vapor l...
n0	1.39932		293.15	Experim...
n0	1.39890		293.15	Solubil...
n0	1.39930		293.15	Liquid-...
n0	1.39930		293.15	Separat...
n0	1.39920		293.15	Vapor L...
n0	1.39970		293.15	Densiti...
n0	1.39920		293.15	Vapor L...
n0	1.39920		293.15	Limitin...
n0	1.39930		293.20	Vapor L...
n0	1.39830		293.20	Liquid-...
n0	1.39930		293.20	Vapor L...
n0	1.39740		298.15	Excess ...
n0	1.39680		298.15	Thermod...
n0	1.39600		298.15	Phase E...
n0	1.39780		298.15	Densiti...
n0	1.39729		298.15	Thermop...
n0	1.39720		298.15	Vapor L...
n0	1.39640		298.15	Applica...
n0	1.39726		298.15	Experim...
n0	1.39747		298.15	Densiti...
n0	1.39830		298.15	Physico...
n0	1.39730		298.15	Density...
n0	1.39730		298.15	Isother...
n0	1.39720		298.15	Propert...
n0	1.39733		298.15	Volumet...
n0	1.39720		298.15	Thermod...
n0	1.39700		298.15	Excess ...
n0	1.39733		298.15	Volumet...
n0	1.39680		298.15	Thermod...
n0	1.39886		298.15	Atmosph...
n0	1.39730		298.15	Isobari...
n0	1.39730		298.15	Experim...
n0	1.39700		298.15	Densiti...
n0	1.39730		298.15	Excess ...
n0	1.39730		298.15	Volumet...
n0	1.39740		298.15	Excess ...
n0	1.39686		298.15	Liquid-...
n0	1.39740		298.15	(Vapor ...
n0	1.39950		298.15	Investi...
n0	1.39740		298.15	Refract...
n0	1.39720		298.15	Effect ...
n0	1.39740		298.15	Excess ...
n0	1.39830		298.15	Density...
n0	1.39730		298.15	Density...
n0	1.39740		298.15	Excess ...
n0	1.39732		298.15	Isobari...
n0	1.39700		298.15	Experim...
n0	1.39760		298.15	Isobari...
n0	1.39740		298.15	Activit...
n0	1.39730		298.15	Isobari...
n0	1.39800		298.15	Bubble ...
n0	1.39740		298.15	Bubble-...
n0	1.39720		298.15	Excess ...
n0	1.39730		298.15	Experim...
n0	1.39680		298.20	Tie lin...
n0	1.39523		303.15	Experim...
n0	1.39530		303.15	Refract...
n0	1.39523		303.15	Experim...
n0	1.39550		303.15	Density...
n0	1.39549		303.15	Densiti...
n0	1.39460		303.15	Measure...
n0	1.39620		303.15	Experim...
n0	1.39590		303.15	Physico...
n0	1.39440		303.15	Thermod...
n0	1.39440		303.15	Thermod...
n0	1.39479		303.15	Density...
n0	1.39500		303.15	Densiti...
n0	1.39520		303.20	Experim...
n0	1.39318		308.15	Experim...
n0	1.39230		308.15	Thermod...
n0	1.39300		308.15	Densiti...
n0	1.39400		308.15	Physico...
n0	1.39318		308.15	Experim...
n0	1.39370		308.15	Density...
n0	1.39330		308.15	Refract...
n0	1.39230		308.15	Thermod...
n0	1.39342		308.15	Densiti...
n0	1.39320		308.15	Excess ...
n0	1.39138		313.15	Densiti...
n0	1.39100		313.15	Densiti...
n0	1.39110		313.15	Experim...
n0	1.39130		313.15	Refract...
n0	1.39110		313.15	Experim...
n0	1.39114		313.15	Thermop...
n0	1.38901		318.15	Experim...
n0	1.38901		318.15	Experim...
n0	1.38930		318.15	Refract...
n0	1.38920		318.20	Experim...
n0	1.38688		323.15	Experim...
n0	1.38688		323.15	Experim...
ρl	[752.08; 817.21]	kg/m3	[283.15; 363.15]
T(K) Liquid Density (kg/m3) 750 760 770 780 790 800 810 820 300 320 340 360
ρl	817.07	kg/m3	283.15	Densiti...
ρl	817.18	kg/m3	283.15	Excess ...
ρl	817.15	kg/m3	283.15	Volumet...
ρl	817.18	kg/m3	283.15	Volumet...
ρl	817.11	kg/m3	283.15	Excess ...
ρl	817.10	kg/m3	283.15	Ionic a...
ρl	817.21	kg/m3	283.15	Effects...
ρl	813.37	kg/m3	288.15	Influen...
ρl	813.41	kg/m3	288.15	Volumet...
ρl	813.32	kg/m3	288.15	Densiti...
ρl	813.77	kg/m3	288.15	Excess ...
ρl	813.37	kg/m3	288.15	Experim...
ρl	813.60	kg/m3	288.15	Excess ...
ρl	813.34	kg/m3	288.15	Ionic a...
ρl	813.40	kg/m3	288.15	Volumet...
ρl	813.35	kg/m3	288.15	Densiti...
ρl	813.38	kg/m3	288.15	Volumet...
ρl	813.46	kg/m3	288.15	Volumet...
ρl	813.37	kg/m3	288.15	Tempera...
ρl	809.60	kg/m3	293.00	Fluid-P...
ρl	809.60	kg/m3	293.00	Fluid-P...
ρl	810.00	kg/m3	293.00	KDB
ρl	810.00	kg/m3	293.15	Density...
ρl	809.56	kg/m3	293.15	Densiti...
ρl	809.69	kg/m3	293.15	Densiti...
ρl	809.55	kg/m3	293.15	Ionic a...
ρl	809.66	kg/m3	293.15	Volumet...
ρl	809.59	kg/m3	293.15	Volumet...
ρl	809.60	kg/m3	293.15	Volumet...
ρl	809.57	kg/m3	293.15	Experim...
ρl	809.80	kg/m3	293.15	Isother...
ρl	809.53	kg/m3	293.15	Volumet...
ρl	809.78	kg/m3	293.15	Excess ...
ρl	809.50	kg/m3	293.15	Isobari...
ρl	809.81	kg/m3	293.15	Molecul...
ρl	809.72	kg/m3	293.15	Propert...
ρl	809.65	kg/m3	293.15	Effects...
ρl	809.50	kg/m3	293.15	Densiti...
ρl	809.57	kg/m3	293.15	Influen...
ρl	809.78	kg/m3	293.15	Density...
ρl	809.84	kg/m3	293.15	Density...
ρl	809.50	kg/m3	293.15	Three B...
ρl	809.54	kg/m3	293.15	Osmotic...
ρl	809.89	kg/m3	293.15	Thermod...
ρl	809.75	kg/m3	293.15	(Liquid...
ρl	809.82	kg/m3	293.15	Thermod...
ρl	809.77	kg/m3	293.15	Volumet...
ρl	809.62	kg/m3	293.15	Volumet...
ρl	809.52	kg/m3	293.15	Thermod...
ρl	809.53	kg/m3	293.15	Intermo...
ρl	809.52	kg/m3	293.15	Densiti...
ρl	809.57	kg/m3	293.15	Tempera...
ρl	809.01	kg/m3	293.15	Densiti...
ρl	810.00	kg/m3	293.15	Liquid-...
ρl	809.49	kg/m3	293.15	Investi...
ρl	809.55	kg/m3	293.15	Densiti...
ρl	809.50	kg/m3	293.15	Measure...
ρl	809.61	kg/m3	293.15	Speed o...
ρl	809.38	kg/m3	293.20	Liquid-...
ρl	806.00	kg/m3	298.00	Compara...
ρl	805.70	kg/m3	298.00	Fluid-P...
ρl	805.70	kg/m3	298.00	Fluid-P...
ρl	805.81	kg/m3	298.15	Speed o...
ρl	805.80	kg/m3	298.15	Excess ...
ρl	805.98	kg/m3	298.15	A syste...
ρl	805.88	kg/m3	298.15	Liquid-...
ρl	806.04	kg/m3	298.15	Measure...
ρl	805.77	kg/m3	298.15	Isobari...
ρl	805.20	kg/m3	298.15	Liquid-...
ρl	805.87	kg/m3	298.15	Densiti...
ρl	805.82	kg/m3	298.15	Excess ...
ρl	805.80	kg/m3	298.15	Bubble ...
ρl	805.50	kg/m3	298.15	Solubil...
ρl	805.79	kg/m3	298.15	Excess ...
ρl	805.99	kg/m3	298.15	Thermod...
ρl	805.78	kg/m3	298.15	Phase b...
ρl	805.88	kg/m3	298.15	Densiti...
ρl	809.50	kg/m3	298.15	Measure...
ρl	805.75	kg/m3	298.15	Physica...
ρl	805.94	kg/m3	298.15	Isobari...
ρl	805.64	kg/m3	298.15	Apparen...
ρl	805.60	kg/m3	298.15	Volumet...
ρl	805.76	kg/m3	298.15	Densiti...
ρl	805.70	kg/m3	298.15	Densiti...
ρl	806.00	kg/m3	298.15	Isobari...
ρl	805.98	kg/m3	298.15	Excess ...
ρl	806.00	kg/m3	298.15	Thermod...
ρl	798.06	kg/m3	298.15	Extract...
ρl	805.85	kg/m3	298.15	Isother...
ρl	805.78	kg/m3	298.15	Liquid ...
ρl	806.47	kg/m3	298.15	Thermod...
ρl	807.96	kg/m3	298.15	Tie-Lin...
ρl	806.14	kg/m3	298.15	Excess ...
ρl	806.03	kg/m3	298.15	Density...
ρl	805.80	kg/m3	298.15	Surface...
ρl	805.70	kg/m3	298.15	Density...
ρl	805.95	kg/m3	298.15	Density...
ρl	805.76	kg/m3	298.15	Influen...
ρl	805.95	kg/m3	298.15	FT-IR s...
ρl	805.76	kg/m3	298.15	Experim...
ρl	805.71	kg/m3	298.15	Excess ...
ρl	805.95	kg/m3	298.15	Densiti...
ρl	805.90	kg/m3	298.15	Thermod...
ρl	805.71	kg/m3	298.15	ACSExce...
ρl	805.99	kg/m3	298.15	Molecul...
ρl	806.05	kg/m3	298.15	Excess ...
ρl	805.71	kg/m3	298.15	Thermop...
ρl	805.76	kg/m3	298.15	Experim...
ρl	805.79	kg/m3	298.15	A combi...
ρl	805.50	kg/m3	298.15	Solubil...
ρl	805.70	kg/m3	298.15	Volumet...
ρl	805.90	kg/m3	298.15	Isother...
ρl	805.80	kg/m3	298.15	Apparen...
ρl	805.77	kg/m3	298.15	Volumet...
ρl	805.92	kg/m3	298.15	Propert...
ρl	805.74	kg/m3	298.15	Excess ...
ρl	809.50	kg/m3	298.15	Topolog...
ρl	805.75	kg/m3	298.15	Excess ...
ρl	805.79	kg/m3	298.15	Measure...
ρl	806.10	kg/m3	298.15	Solubil...
ρl	805.80	kg/m3	298.15	Revisio...
ρl	805.75	kg/m3	298.15	Densiti...
ρl	805.60	kg/m3	298.15	Densiti...
ρl	805.74	kg/m3	298.15	Ionic a...
ρl	805.78	kg/m3	298.15	Volumet...
ρl	805.84	kg/m3	298.15	Volumet...
ρl	805.67	kg/m3	298.15	Mixing ...
ρl	805.90	kg/m3	298.15	Dynamic...
ρl	805.95	kg/m3	298.15	Thermod...
ρl	805.92	kg/m3	298.15	Densiti...
ρl	806.00	kg/m3	298.15	Thermod...
ρl	805.77	kg/m3	298.15	Effect ...
ρl	805.92	kg/m3	298.15	Volumet...
ρl	806.27	kg/m3	298.15	Effect ...
ρl	806.00	kg/m3	298.15	Density...
ρl	805.76	kg/m3	298.15	Liquid ...
ρl	805.80	kg/m3	298.15	Experim...
ρl	805.85	kg/m3	298.15	Binary ...
ρl	805.71	kg/m3	298.15	Thermod...
ρl	805.87	kg/m3	298.15	Binary ...
ρl	805.72	kg/m3	298.15	Excess ...
ρl	805.76	kg/m3	298.15	Tempera...
ρl	806.14	kg/m3	298.15	Speeds ...
ρl	805.65	kg/m3	298.15	Investi...
ρl	805.80	kg/m3	298.15	Volumet...
ρl	805.98	kg/m3	298.15	Densiti...
ρl	805.88	kg/m3	298.20	Liquid-...
ρl	806.01	kg/m3	298.20	Isother...
ρl	807.96	kg/m3	298.20	Phase e...
ρl	805.81	kg/m3	298.20	Liquid-...
ρl	802.00	kg/m3	303.00	Compara...
ρl	801.90	kg/m3	303.00	Fluid-P...
ρl	801.90	kg/m3	303.00	Fluid-P...
ρl	801.97	kg/m3	303.15	Speed o...
ρl	804.00	kg/m3	303.15	Study o...
ρl	801.91	kg/m3	303.15	Densiti...
ρl	801.92	kg/m3	303.15	Tempera...
ρl	801.87	kg/m3	303.15	Thermod...
ρl	802.00	kg/m3	303.15	Intermo...
ρl	803.68	kg/m3	303.15	Investi...
ρl	802.22	kg/m3	303.15	Thermod...
ρl	802.00	kg/m3	303.15	Density...
ρl	802.04	kg/m3	303.15	Densiti...
ρl	801.92	kg/m3	303.15	Influen...
ρl	801.94	kg/m3	303.15	Densiti...
ρl	802.42	kg/m3	303.15	Effect ...
ρl	802.19	kg/m3	303.15	Density...
ρl	802.15	kg/m3	303.15	Thermod...
ρl	801.98	kg/m3	303.15	Excess ...
ρl	802.03	kg/m3	303.15	Excess ...
ρl	801.92	kg/m3	303.15	Isobari...
ρl	801.96	kg/m3	303.15	Volumet...
ρl	801.92	kg/m3	303.15	Volumet...
ρl	802.00	kg/m3	303.15	Volumet...
ρl	801.99	kg/m3	303.15	Densiti...
ρl	801.90	kg/m3	303.15	Ionic a...
ρl	801.94	kg/m3	303.15	Volumet...
ρl	801.91	kg/m3	303.15	Vapor-l...
ρl	802.06	kg/m3	303.15	Densiti...
ρl	802.01	kg/m3	303.15	Density...
ρl	802.10	kg/m3	303.15	Density...
ρl	801.92	kg/m3	303.15	Studies...
ρl	801.90	kg/m3	303.15	Volumet...
ρl	801.90	kg/m3	303.15	Densiti...
ρl	802.08	kg/m3	303.15	Propert...
ρl	801.86	kg/m3	303.15	Volumet...
ρl	801.87	kg/m3	303.15	Densiti...
ρl	801.92	kg/m3	303.15	Experim...
ρl	802.11	kg/m3	303.15	FT-IR s...
ρl	802.13	kg/m3	303.15	A syste...
ρl	802.16	kg/m3	303.15	Densiti...
ρl	802.00	kg/m3	303.15	Effects...
ρl	802.10	kg/m3	303.15	Viscous...
ρl	802.14	kg/m3	303.15	Molecul...
ρl	801.99	kg/m3	303.15	Volumet...
ρl	798.00	kg/m3	308.00	Compara...
ρl	798.10	kg/m3	308.15	Speed o...
ρl	798.12	kg/m3	308.15	Volumet...
ρl	798.28	kg/m3	308.15	Densiti...
ρl	798.09	kg/m3	308.15	Volumet...
ρl	798.25	kg/m3	308.15	A syste...
ρl	798.05	kg/m3	308.15	Experim...
ρl	798.05	kg/m3	308.15	Experim...
ρl	798.20	kg/m3	308.15	Isother...
ρl	798.21	kg/m3	308.15	Propert...
ρl	798.00	kg/m3	308.15	Density...
ρl	798.00	kg/m3	308.15	Densiti...
ρl	798.23	kg/m3	308.15	Density...
ρl	798.18	kg/m3	308.15	Densiti...
ρl	798.20	kg/m3	308.15	Densiti...
ρl	798.14	kg/m3	308.15	Density...
ρl	797.99	kg/m3	308.15	Volumet...
ρl	798.03	kg/m3	308.15	Ionic a...
ρl	798.54	kg/m3	308.15	Effect ...
ρl	798.26	kg/m3	308.15	Molecul...
ρl	798.14	kg/m3	308.15	Volumet...
ρl	798.28	kg/m3	308.15	Thermod...
ρl	798.38	kg/m3	308.15	Density...
ρl	798.05	kg/m3	308.15	Tempera...
ρl	798.05	kg/m3	308.15	Volumet...
ρl	798.06	kg/m3	308.15	Physica...
ρl	798.00	kg/m3	308.15	Thermod...
ρl	798.06	kg/m3	308.15	Effect ...
ρl	798.05	kg/m3	308.15	Influen...
ρl	800.50	kg/m3	308.15	Investi...
ρl	798.09	kg/m3	308.15	Densiti...
ρl	798.04	kg/m3	308.15	Densiti...
ρl	798.01	kg/m3	308.15	Osmotic...
ρl	798.24	kg/m3	308.15	FT-IR s...
ρl	794.00	kg/m3	313.00	Compara...
ρl	794.19	kg/m3	313.15	Speed o...
ρl	794.15	kg/m3	313.15	Tempera...
ρl	794.34	kg/m3	313.15	Excess ...
ρl	794.13	kg/m3	313.15	Ionic a...
ρl	794.15	kg/m3	313.15	Influen...
ρl	794.13	kg/m3	313.15	Densiti...
ρl	794.20	kg/m3	313.15	Densiti...
ρl	794.10	kg/m3	313.15	Thermod...
ρl	794.34	kg/m3	313.15	Densiti...
ρl	794.18	kg/m3	313.15	Volumet...
ρl	794.24	kg/m3	313.15	Volumet...
ρl	794.22	kg/m3	313.15	Volumet...
ρl	794.14	kg/m3	313.15	Volumet...
ρl	794.40	kg/m3	313.15	Excess ...
ρl	794.70	kg/m3	313.15	Intermo...
ρl	794.22	kg/m3	313.15	Density...
ρl	794.31	kg/m3	313.15	Density...
ρl	794.26	kg/m3	313.15	Densiti...
ρl	794.00	kg/m3	313.15	Density...
ρl	794.37	kg/m3	313.15	Thermod...
ρl	794.27	kg/m3	313.15	Densiti...
ρl	794.50	kg/m3	313.15	Densiti...
ρl	794.62	kg/m3	313.15	Effect ...
ρl	794.21	kg/m3	313.15	Effects...
ρl	794.10	kg/m3	313.15	Volumet...
ρl	794.37	kg/m3	313.15	Densiti...
ρl	794.30	kg/m3	313.15	Propert...
ρl	794.38	kg/m3	313.15	Molecul...
ρl	794.12	kg/m3	313.15	Excess ...
ρl	794.11	kg/m3	313.15	Investi...
ρl	794.10	kg/m3	313.15	Densiti...
ρl	794.15	kg/m3	313.15	Experim...
ρl	794.18	kg/m3	313.15	Excess ...
ρl	794.49	kg/m3	313.15	Excess ...
ρl	793.78	kg/m3	313.20	Liquid-...
ρl	790.24	kg/m3	318.15	Speed o...
ρl	790.43	kg/m3	318.15	Thermod...
ρl	790.42	kg/m3	318.15	Densiti...
ρl	790.23	kg/m3	318.15	Experim...
ρl	790.27	kg/m3	318.15	Thermod...
ρl	790.18	kg/m3	318.15	Ionic a...
ρl	790.21	kg/m3	318.15	Experim...
ρl	790.20	kg/m3	318.15	Volumet...
ρl	790.10	kg/m3	318.15	Density...
ρl	790.18	kg/m3	318.15	Volumet...
ρl	790.30	kg/m3	318.15	Densiti...
ρl	790.15	kg/m3	318.15	Densiti...
ρl	790.28	kg/m3	318.15	Volumet...
ρl	790.28	kg/m3	318.15	Density...
ρl	790.19	kg/m3	318.15	Volumet...
ρl	790.19	kg/m3	318.15	Effect ...
ρl	790.18	kg/m3	318.15	Densiti...
ρl	790.27	kg/m3	318.15	Densiti...
ρl	790.23	kg/m3	318.15	Volumet...
ρl	790.65	kg/m3	318.15	Effect ...
ρl	790.22	kg/m3	318.15	Physica...
ρl	786.25	kg/m3	323.15	Speed o...
ρl	786.67	kg/m3	323.15	Densiti...
ρl	786.30	kg/m3	323.15	Densiti...
ρl	786.19	kg/m3	323.15	Volumet...
ρl	786.15	kg/m3	323.15	Osmotic...
ρl	786.44	kg/m3	323.15	Thermod...
ρl	786.29	kg/m3	323.15	Density...
ρl	787.00	kg/m3	323.15	Density...
ρl	786.32	kg/m3	323.15	Osmotic...
ρl	786.16	kg/m3	323.15	Densiti...
ρl	786.64	kg/m3	323.15	Effect ...
ρl	786.21	kg/m3	323.15	Volumet...
ρl	786.21	kg/m3	323.15	Volumet...
ρl	786.23	kg/m3	323.15	Volumet...
ρl	786.41	kg/m3	323.15	Densiti...
ρl	786.32	kg/m3	323.15	Densiti...
ρl	786.62	kg/m3	323.15	Vapor-l...
ρl	786.24	kg/m3	323.15	Experim...
ρl	786.18	kg/m3	323.15	Densiti...
ρl	786.29	kg/m3	323.15	Densiti...
ρl	786.29	kg/m3	323.15	Volumet...
ρl	782.25	kg/m3	328.15	Densiti...
ρl	782.12	kg/m3	328.15	Densiti...
ρl	782.48	kg/m3	328.15	Excess ...
ρl	782.02	kg/m3	328.15	Densiti...
ρl	782.32	kg/m3	328.15	Excess ...
ρl	782.15	kg/m3	328.15	Effect ...
ρl	782.14	kg/m3	328.15	Volumet...
ρl	782.17	kg/m3	328.15	Volumet...
ρl	782.11	kg/m3	328.15	Excess ...
ρl	782.27	kg/m3	328.15	Densiti...
ρl	782.12	kg/m3	328.15	Densiti...
ρl	778.18	kg/m3	333.15	Densiti...
ρl	778.03	kg/m3	333.15	Volumet...
ρl	778.01	kg/m3	333.15	Densiti...
ρl	778.06	kg/m3	333.15	Volumet...
ρl	778.01	kg/m3	333.15	Densiti...
ρl	778.16	kg/m3	333.15	Densiti...
ρl	777.81	kg/m3	333.15	Densiti...
ρl	778.09	kg/m3	333.15	Densiti...
ρl	774.03	kg/m3	338.15	Excess ...
ρl	774.03	kg/m3	338.15	Densiti...
ρl	773.89	kg/m3	338.15	Effect ...
ρl	769.80	kg/m3	343.15	Densiti...
ρl	765.49	kg/m3	348.15	Densiti...
ρl	765.48	kg/m3	348.15	Excess ...
ρl	761.12	kg/m3	353.15	Densiti...
ρl	756.64	kg/m3	358.15	Densiti...
ρl	752.08	kg/m3	363.15	Densiti...
ΔfusS	[50.46; 50.79]	J/mol×K	[183.90; 184.50]
ΔfusS	50.46	J/mol×K	183.90	NIST
ΔfusS	50.79	J/mol×K	184.50	NIST
csound,fluid	[1156.90; 1308.19]	m/s	[278.15; 323.15]
T(K) Speed of sound in fluid (m/s) 1150 1200 1250 1300 280 300 320
csound,fluid	1308.19	m/s	278.15	Thermod...
csound,fluid	1292.20	m/s	283.15	Excess ...
csound,fluid	1273.70	m/s	288.15	Excess ...
csound,fluid	1273.51	m/s	288.15	Thermod...
csound,fluid	1282.20	m/s	288.15	Ultraso...
csound,fluid	1262.40	m/s	293.15	Ultraso...
csound,fluid	1256.30	m/s	293.15	Acousti...
csound,fluid	1256.70	m/s	293.15	Acousti...
csound,fluid	1257.00	m/s	293.15	Excess ...
csound,fluid	1244.00	m/s	298.15	Densiti...
csound,fluid	1240.70	m/s	298.15	Excess ...
csound,fluid	1239.29	m/s	298.15	Thermod...
csound,fluid	1242.60	m/s	298.15	Ultraso...
csound,fluid	1241.30	m/s	298.15	Ultraso...
csound,fluid	1241.60	m/s	298.15	Compres...
csound,fluid	1239.80	m/s	298.15	Excess ...
csound,fluid	1225.80	m/s	303.15	Ultraso...
csound,fluid	1222.70	m/s	303.15	Excess ...
csound,fluid	1205.90	m/s	308.15	Excess ...
csound,fluid	1206.50	m/s	308.15	Acousti...
csound,fluid	1205.50	m/s	308.15	Thermod...
csound,fluid	1207.60	m/s	308.15	Ultraso...
csound,fluid	1212.00	m/s	308.15	Densiti...
csound,fluid	1191.40	m/s	313.15	Excess ...
csound,fluid	1189.20	m/s	313.15	Ultraso...
csound,fluid	1170.00	m/s	318.15	Ultraso...
csound,fluid	1172.12	m/s	318.15	Thermod...
csound,fluid	1156.90	m/s	323.15	Acousti...
γ	[0.02; 0.03]	N/m	[283.15; 333.20]
T(K) Surface Tension (N/m) 0.02 0.02 0.02 0.02 0.02 0.03 0.03 300 320
γ	0.03	N/m	283.15	Study o...
γ	0.02	N/m	288.15	Study o...
γ	0.03	N/m	288.15	Study o...
γ	0.02	N/m	288.15	Density...
γ	0.02	N/m	293.15	Surface...
γ	0.02	N/m	293.15	Study o...
γ	0.02	N/m	293.15	Density...
γ	0.02	N/m	293.15	Density...
γ	0.02	N/m	293.20	Surface...
γ	0.03	N/m	293.20	KDB
γ	0.02	N/m	298.00	Surface...
γ	0.02	N/m	298.15	Density...
γ	0.02	N/m	298.15	Study o...
γ	0.02	N/m	298.15	Surface...
γ	0.02	N/m	298.15	Study o...
γ	0.02	N/m	298.15	Concent...
γ	0.02	N/m	303.15	Density...
γ	0.02	N/m	303.15	Study o...
γ	0.02	N/m	303.15	Surface...
γ	0.02	N/m	303.20	Surface...
γ	0.02	N/m	308.15	Study o...
γ	0.02	N/m	308.15	Study o...
γ	0.02	N/m	308.15	Surface...
γ	0.02	N/m	308.15	Density...
γ	0.02	N/m	313.15	Study o...
γ	0.02	N/m	313.15	Surface...
γ	0.02	N/m	313.20	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	323.20	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	[376.95; 390.65]	K	[59.97; 101.40]
P(kPa) Boiling point at given pressure (K) 380 385 390 60 80 100
Tboil	376.95	K	59.97	Isobari...
Tboil	379.65	K	66.66	Isobari...
Tboil	382.05	K	73.37	Isobari...
Tboil	384.35	K	80.04	Isobari...
Tboil	386.45	K	86.71	Isobari...
Tboil	390.65	K	101.40	Isobari...

Datasets

1. Molar heat capacity at constant pressure, J/K/mol (1)
2. Viscosity, Pa*s (1)
3. Refractive index (Na D-line) (2)
4. Mass density, kg/m3 (1)
5. Mass density, kg/m3 (11)
6. Speed of sound, m/s (2)

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

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Molar heat capacity at constant pressure, J/K/mol - Liquid
273.15	100.00	159.50
273.15	5000.00	158.70
273.15	10000.00	158.40
273.15	15000.00	158.20
273.15	20000.00	157.90
273.15	25000.00	157.20
293.15	100.00	175.20
293.15	5000.00	173.90
293.15	10000.00	172.80
293.15	15000.00	173.50
293.15	20000.00	172.10
293.15	25000.00	171.70
313.15	100.00	190.40
313.15	5000.00	189.80
313.15	10000.00	189.00
313.15	15000.00	187.60
313.15	20000.00	186.70
313.15	25000.00	186.00
333.15	100.00	206.60
333.15	5000.00	206.50
333.15	10000.00	204.90
333.15	15000.00	202.00
333.15	20000.00	200.70
333.15	25000.00	199.90
Reference

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
298.15	81.50	0.0026
Reference

Refractive index (Na D-line)

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Refractive index (Na D-line) - Liquid
100.00	298.15	1.3975
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Refractive index (Na D-line) - Liquid
294.15	100.00	1.3978
Reference

Mass density, kg/m3

Fixed		Measured
Temperature, K - Gas	Pressure, kPa - Gas	Mass density, kg/m3 - Gas
528.31	2642.00	113.76
539.69	3127.00	113.76
543.30	3315.00	113.76
546.79	3456.00	113.76
548.15	3531.00	113.76
551.66	3610.00	113.76
558.64	3788.00	113.76
574.48	4178.00	113.76
590.87	4586.00	113.76
605.17	4925.00	113.76
616.28	5197.00	113.76
531.38	2775.00	167.7
543.89	3315.00	167.7
550.45	3647.00	167.7
555.53	3893.00	167.7
557.65	4020.00	167.7
562.14	4275.00	167.7
569.15	4559.00	167.7
580.80	5000.00	167.7
593.16	5452.00	167.7
604.17	5852.00	167.7
616.27	6275.00	167.7
533.03	2834.00	203.9
548.49	3579.00	203.9
555.70	3941.00	203.9
559.33	4118.00	203.9
563.04	4340.00	203.9
568.44	4598.00	203.9
577.73	5059.00	203.9
588.79	5613.00	203.9
600.42	6162.00	203.9
614.97	6834.00	203.9
Reference

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.15	100.00	809.5
293.15	10000.00	816.4
293.15	20000.00	822.9
293.15	30000.00	828.9
293.15	40000.00	834.5
293.15	50000.00	839.8
293.15	60000.00	844.7
293.15	70000.00	849.6
293.15	80000.00	854.2
293.15	90000.00	858.5
293.15	100000.00	862.9
293.15	110000.00	866.7
293.15	120000.00	870.8
293.15	130000.00	874.4
293.15	140000.00	878.1
303.15	100.00	802.0
303.15	10000.00	809.4
303.15	20000.00	816.0
303.15	30000.00	822.3
303.15	40000.00	828.0
303.15	50000.00	833.6
303.15	60000.00	838.7
303.15	70000.00	843.6
303.15	80000.00	848.3
303.15	90000.00	852.7
303.15	100000.00	857.0
303.15	110000.00	861.2
303.15	120000.00	865.0
303.15	130000.00	868.9
303.15	140000.00	872.6
313.15	100.00	794.1
313.15	10000.00	801.6
313.15	20000.00	809.1
313.15	30000.00	815.4
313.15	40000.00	821.4
313.15	50000.00	827.2
313.15	60000.00	832.6
313.15	70000.00	837.8
313.15	80000.00	842.6
313.15	90000.00	847.3
313.15	100000.00	851.6
313.15	110000.00	856.0
313.15	120000.00	860.1
313.15	130000.00	864.0
313.15	140000.00	867.9
323.15	100.00	786.5
323.15	10000.00	794.5
323.15	20000.00	801.7
323.15	30000.00	808.5
323.15	40000.00	815.0
323.15	50000.00	821.0
323.15	60000.00	826.5
323.15	70000.00	831.5
323.15	80000.00	836.3
323.15	90000.00	841.1
323.15	100000.00	845.8
323.15	110000.00	850.1
323.15	120000.00	854.3
323.15	130000.00	858.3
323.15	140000.00	862.1
333.15	100.00	778.3
333.15	10000.00	786.8
333.15	20000.00	794.6
333.15	30000.00	801.7
333.15	40000.00	808.4
333.15	50000.00	814.6
333.15	60000.00	820.3
333.15	70000.00	825.6
333.15	80000.00	830.8
333.15	90000.00	836.0
333.15	100000.00	840.5
333.15	110000.00	844.9
333.15	120000.00	849.0
333.15	130000.00	853.2
333.15	140000.00	857.0
343.15	100.00	769.9
343.15	10000.00	779.0
343.15	20000.00	787.1
343.15	30000.00	794.4
343.15	40000.00	801.3
343.15	50000.00	807.8
343.15	60000.00	813.6
343.15	70000.00	819.3
343.15	80000.00	824.6
343.15	90000.00	829.5
343.15	100000.00	834.4
343.15	110000.00	838.9
343.15	120000.00	843.3
343.15	130000.00	847.5
343.15	140000.00	851.6
353.15	100.00	760.9
353.15	10000.00	770.6
353.15	20000.00	779.2
353.15	30000.00	787.1
353.15	40000.00	794.3
353.15	50000.00	800.9
353.15	60000.00	807.7
353.15	70000.00	813.2
353.15	80000.00	818.9
353.15	90000.00	823.9
353.15	100000.00	828.8
353.15	110000.00	833.5
353.15	120000.00	838.1
353.15	130000.00	842.1
353.15	140000.00	846.5
363.15	100.00	751.9
363.15	10000.00	762.6
363.15	20000.00	771.7
363.15	30000.00	780.1
363.15	40000.00	787.4
363.15	50000.00	794.3
363.15	60000.00	800.9
363.15	70000.00	807.0
363.15	80000.00	812.5
363.15	90000.00	817.9
363.15	100000.00	822.9
363.15	110000.00	827.7
363.15	120000.00	832.4
363.15	130000.00	836.8
363.15	140000.00	841.0
373.15	100.00	742.4
373.15	10000.00	753.4
373.15	20000.00	763.3
373.15	30000.00	772.2
373.15	40000.00	780.0
373.15	50000.00	787.2
373.15	60000.00	793.8
373.15	70000.00	800.2
373.15	80000.00	805.8
373.15	90000.00	811.5
373.15	100000.00	817.0
373.15	110000.00	821.9
373.15	120000.00	826.3
373.15	130000.00	831.0
373.15	140000.00	835.3
383.15	100.00	732.2
383.15	10000.00	744.7
383.15	20000.00	754.6
383.15	30000.00	764.3
383.15	40000.00	772.2
383.15	50000.00	779.6
383.15	60000.00	786.6
383.15	70000.00	793.2
383.15	80000.00	799.1
383.15	90000.00	804.9
383.15	100000.00	810.3
383.15	110000.00	815.4
383.15	120000.00	820.4
383.15	130000.00	825.0
383.15	140000.00	829.6
393.15	10000.00	735.3
393.15	20000.00	746.4
393.15	30000.00	755.9
393.15	40000.00	764.9
393.15	50000.00	772.3
393.15	60000.00	779.6
393.15	70000.00	786.3
393.15	80000.00	792.8
393.15	90000.00	798.8
393.15	100000.00	804.3
393.15	110000.00	809.7
393.15	120000.00	814.7
393.15	130000.00	819.3
393.15	140000.00	823.9
403.15	10000.00	725.6
403.15	20000.00	737.3
403.15	30000.00	747.7
403.15	40000.00	756.9
403.15	50000.00	765.4
403.15	60000.00	772.8
403.15	70000.00	779.9
403.15	80000.00	786.5
403.15	90000.00	792.6
403.15	100000.00	798.5
403.15	110000.00	803.9
403.15	120000.00	809.1
403.15	130000.00	814.1
403.15	140000.00	819.3
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
313.10	1013.00	794.97
313.10	2008.00	795.76
313.10	3007.00	796.55
313.10	3990.00	797.33
313.10	5000.00	798.11
313.10	6014.00	798.9
313.10	7006.00	799.69
313.10	8016.00	800.47
313.10	9008.00	801.23
313.10	9996.00	801.97
313.10	11012.00	802.72
313.10	12008.00	803.48
313.10	13036.00	804.23
313.10	14009.00	804.93
313.10	15034.00	805.67
313.10	16014.00	806.36
313.10	17013.00	807.07
313.10	18011.00	807.76
313.10	19027.00	808.46
313.10	20015.00	809.14
313.10	21034.00	809.84
313.10	22060.00	810.53
313.10	23039.00	811.19
313.10	24049.00	811.9
313.10	25048.00	812.56
323.08	1040.00	787.23
323.08	2043.00	788.06
323.08	3005.00	788.88
323.08	4009.00	789.7
323.08	5014.00	790.53
323.08	6024.00	791.38
323.08	7062.00	792.21
323.08	8033.00	792.99
323.08	9025.00	793.79
323.08	10008.00	794.58
323.08	11020.00	795.36
323.08	12027.00	796.15
323.08	13044.00	796.95
323.08	14035.00	797.69
323.08	15055.00	798.46
323.08	16063.00	799.21
323.08	17039.00	799.93
323.08	18057.00	800.67
323.08	18995.00	801.37
323.08	20045.00	802.11
323.08	21090.00	802.85
323.08	22039.00	803.52
323.08	23078.00	804.27
323.08	24010.00	804.94
323.08	25055.00	805.68
332.95	1095.00	779.28
332.95	2064.00	780.15
332.95	3035.00	781.02
332.95	4039.00	781.89
332.95	5007.00	782.76
332.95	6035.00	783.65
332.95	7048.00	784.53
332.95	8021.00	785.37
332.95	9035.00	786.23
332.95	10030.00	787.06
332.95	11057.00	787.9
332.95	12026.00	788.71
332.95	13041.00	789.54
332.95	14034.00	790.33
332.95	15074.00	791.16
332.95	16022.00	791.89
332.95	16957.00	792.61
332.95	18103.00	793.49
332.95	19053.00	794.22
332.95	20044.00	794.97
332.95	21090.00	795.75
332.95	21974.00	796.4
332.95	22960.00	797.13
332.95	24014.00	797.92
332.95	25045.00	798.67
342.89	1021.00	771.26
342.89	2060.00	772.26
342.89	3051.00	773.2
342.89	4044.00	774.13
342.89	5014.00	775.03
342.89	6024.00	775.96
342.89	7050.00	776.88
342.89	8037.00	777.76
342.89	9052.00	778.65
342.89	10057.00	779.53
342.89	11053.00	780.38
342.89	12027.00	781.22
342.89	13077.00	782.09
342.89	14026.00	782.86
342.89	15080.00	783.73
342.89	16028.00	784.48
342.89	17031.00	785.27
342.89	18020.00	786.04
342.89	19009.00	786.8
342.89	20030.00	787.58
342.89	21066.00	788.35
342.89	21978.00	789.03
342.89	23061.00	789.83
342.89	24031.00	790.55
342.89	25045.00	791.3
352.76	1033.00	762.72
352.76	2075.00	763.8
352.76	3038.00	764.75
352.76	4004.00	765.74
352.76	5017.00	766.75
352.76	6042.00	767.75
352.76	7041.00	768.72
352.76	8024.00	769.64
352.76	9042.00	770.61
352.76	10044.00	771.56
352.76	11026.00	772.44
352.76	12073.00	773.4
352.76	13002.00	774.25
352.76	14050.00	775.17
352.76	15000.00	776.03
352.76	15999.00	776.89
352.76	17008.00	777.76
352.76	18066.00	778.65
352.76	19002.00	779.43
352.76	20014.00	780.28
352.76	21043.00	781.12
352.76	22024.00	781.94
352.76	23025.00	782.75
352.76	24015.00	783.56
352.76	25100.00	784.44
362.68	1031.00	753.17
362.68	2065.00	754.33
362.68	3038.00	755.4
362.68	4026.00	756.45
362.68	5050.00	757.54
362.68	6018.00	758.55
362.68	6995.00	759.56
362.68	8100.00	760.7
362.68	9002.00	761.62
362.68	10021.00	762.62
362.68	10995.00	763.58
362.68	12059.00	764.62
362.68	13056.00	765.56
362.68	14029.00	766.47
362.68	15024.00	767.42
362.68	16010.00	768.33
362.68	17020.00	769.25
362.68	18041.00	770.16
362.68	19031.00	771.05
362.68	20045.00	771.93
362.68	21016.00	772.76
362.68	22022.00	773.64
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
278.15	100.00	820.9
278.15	1000.00	821.6
278.15	5000.00	824.4
278.15	10000.00	827.7
278.15	15000.00	830.9
278.15	20000.00	834.0
278.15	25000.00	837.0
278.15	30000.00	839.9
278.15	35000.00	842.7
278.15	40000.00	845.4
278.15	45000.00	848.1
278.15	50000.00	850.7
278.15	55000.00	853.2
278.15	60000.00	855.6
288.15	100.00	813.5
288.15	1000.00	814.1
288.15	5000.00	817.0
288.15	10000.00	820.5
288.15	15000.00	823.9
288.15	20000.00	827.2
288.15	25000.00	830.3
288.15	30000.00	833.2
288.15	35000.00	836.2
288.15	40000.00	839.0
288.15	45000.00	841.7
288.15	50000.00	844.4
288.15	55000.00	846.8
288.15	60000.00	849.4
298.15	100.00	805.8
298.15	1000.00	806.6
298.15	5000.00	809.6
298.15	10000.00	813.3
298.15	15000.00	816.8
298.15	20000.00	820.2
298.15	25000.00	823.5
298.15	30000.00	826.6
298.15	35000.00	829.6
298.15	40000.00	832.6
298.15	45000.00	835.4
298.15	50000.00	838.2
298.15	55000.00	840.9
298.15	60000.00	843.3
308.15	100.00	798.0
308.15	1000.00	798.8
308.15	5000.00	802.0
308.15	10000.00	805.9
308.15	15000.00	809.5
308.15	20000.00	813.0
308.15	25000.00	816.4
308.15	30000.00	819.7
308.15	35000.00	822.8
308.15	40000.00	825.9
308.15	45000.00	828.8
308.15	50000.00	831.7
308.15	55000.00	834.5
308.15	60000.00	837.0
318.15	100.00	790.3
318.15	1000.00	791.1
318.15	5000.00	794.5
318.15	10000.00	798.5
318.15	15000.00	802.4
318.15	20000.00	805.6
318.15	25000.00	809.5
318.15	30000.00	812.9
318.15	35000.00	816.1
318.15	40000.00	819.3
318.15	45000.00	822.4
318.15	50000.00	825.3
318.15	55000.00	828.2
318.15	60000.00	830.9
328.15	100.00	782.3
328.15	1000.00	783.1
328.15	5000.00	786.7
328.15	10000.00	790.9
328.15	15000.00	795.0
328.15	20000.00	798.8
328.15	25000.00	802.4
328.15	30000.00	806.0
328.15	35000.00	809.4
328.15	40000.00	812.7
328.15	45000.00	815.8
328.15	50000.00	818.9
328.15	55000.00	821.8
328.15	60000.00	824.6
338.15	100.00	774.0
338.15	1000.00	774.9
338.15	5000.00	778.7
338.15	10000.00	783.2
338.15	15000.00	787.4
338.15	20000.00	791.4
338.15	25000.00	795.3
338.15	30000.00	799.0
338.15	35000.00	802.5
338.15	40000.00	805.9
338.15	45000.00	809.2
338.15	50000.00	812.4
338.15	55000.00	815.4
338.15	60000.00	818.4
348.15	100.00	765.6
348.15	1000.00	766.3
348.15	5000.00	770.5
348.15	10000.00	775.3
348.15	15000.00	779.8
348.15	20000.00	784.0
348.15	25000.00	788.0
348.15	30000.00	791.8
348.15	35000.00	795.6
348.15	40000.00	799.1
348.15	45000.00	802.5
348.15	50000.00	805.8
348.15	55000.00	809.0
348.15	60000.00	811.9
358.15	100.00	756.6
358.15	1000.00	757.7
358.15	5000.00	761.7
358.15	10000.00	767.0
358.15	15000.00	771.7
358.15	20000.00	776.2
358.15	25000.00	780.4
358.15	30000.00	784.4
358.15	35000.00	788.3
358.15	40000.00	792.0
358.15	45000.00	795.5
358.15	50000.00	799.0
358.15	55000.00	802.3
358.15	60000.00	805.3
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
100.00	302.90	802.0
1020.00	302.90	802.7
2010.00	302.90	803.4
3010.00	302.90	804.1
4000.00	302.90	804.9
5010.00	302.90	805.7
6000.00	302.90	806.4
7020.00	302.90	807.2
8010.00	302.90	807.9
9020.00	302.90	808.7
10020.00	302.90	809.4
100.00	323.10	785.6
1010.00	323.10	786.6
2020.00	323.10	787.5
3010.00	323.10	788.3
4000.00	323.10	789.2
5020.00	323.10	790.0
6020.00	323.10	790.9
7000.00	323.10	791.7
8010.00	323.10	792.5
9020.00	323.10	793.3
10020.00	323.10	794.2
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	805.95
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	81.50	806.07
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.63	80.00	817.19
283.64	1000.00	817.88
283.63	5000.00	820.7
283.66	10000.00	824.01
283.66	20000.00	830.39
283.65	30000.00	836.43
283.64	40000.00	842.03
283.64	60000.00	852.39
283.65	80000.00	861.72
283.64	100000.00	870.33
303.45	100.00	801.81
303.45	1000.00	802.54
303.46	5000.00	805.65
303.46	10000.00	809.35
303.47	20000.00	816.29
303.47	30000.00	822.84
303.47	40000.00	828.87
303.47	60000.00	839.95
303.48	80010.00	849.82
303.48	100000.00	858.94
323.26	100.00	786.36
323.25	1000.00	787.19
323.26	5000.00	790.63
323.27	10000.00	794.68
323.27	20000.00	802.33
323.27	30000.00	809.41
323.28	40000.00	816.0
323.28	60000.00	827.77
323.28	80000.00	838.31
323.28	100000.00	847.65
343.03	100.00	769.54
343.03	1000.00	770.45
343.04	5000.00	774.32
343.04	10000.00	778.88
343.05	20000.00	787.37
343.05	30000.00	795.06
343.05	40000.00	802.13
343.05	60000.00	814.83
343.05	80000.00	826.08
343.05	100000.00	836.2
362.68	100.00	752.67
362.68	1000.00	753.64
362.69	5000.00	758.03
362.69	10000.00	763.16
362.69	20000.00	772.56
362.68	30000.00	781.04
362.70	40000.00	788.67
362.70	60000.00	802.36
362.71	80000.00	814.44
362.71	100000.00	825.18
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.12	2010.00	806.8
298.12	3910.00	808.2
298.12	6020.00	809.8
298.12	8030.00	811.2
298.12	9910.00	812.5
298.13	13010.00	814.6
298.12	16020.00	816.6
298.12	19030.00	818.5
298.12	22000.00	820.4
298.12	25020.00	822.3
298.12	28000.00	824.0
298.12	30010.00	825.1
303.15	2010.00	803.3
303.15	4000.00	804.8
303.15	5980.00	806.3
303.15	8010.00	807.8
303.15	9990.00	809.2
303.15	12990.00	811.3
303.15	15990.00	813.3
303.16	19000.00	815.3
303.15	22010.00	817.3
303.15	25010.00	819.1
303.15	27970.00	820.9
303.15	29990.00	822.1
313.16	1990.00	795.5
313.16	3980.00	797.1
313.16	5990.00	798.7
313.16	7980.00	800.2
313.15	10020.00	801.8
313.15	12980.00	803.9
313.16	15980.00	806.1
313.16	19010.00	808.2
313.15	22020.00	810.2
313.15	25010.00	812.2
313.16	27990.00	814.1
313.16	29990.00	815.3
323.14	2000.00	787.9
323.14	3920.00	789.6
323.14	6030.00	791.3
323.14	8000.00	792.9
323.14	10020.00	794.5
323.14	13040.00	796.9
323.14	16050.00	799.2
323.14	19000.00	801.3
323.14	21990.00	803.4
323.14	24970.00	805.5
323.14	28000.00	807.5
323.14	29970.00	808.8
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.15	100.00	809.28
293.15	5000.00	813.04
293.15	10000.00	816.54
293.15	15000.00	819.83
293.15	20000.00	822.97
293.15	25000.00	826.0
293.15	30000.00	828.99
293.15	35000.00	831.99
303.15	100.00	801.9
303.15	5000.00	806.0
303.15	10000.00	809.77
303.15	15000.00	813.26
303.15	20000.00	816.52
303.15	25000.00	819.61
303.15	30000.00	822.58
303.15	35000.00	825.48
313.15	100.00	794.32
313.15	5000.00	798.42
313.15	10000.00	802.22
313.15	15000.00	805.8
313.15	20000.00	809.2
313.15	25000.00	812.49
313.15	30000.00	815.73
313.15	35000.00	818.97
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.15	550.80	818.14
283.15	11959.00	825.705
283.15	18047.00	829.455
283.15	32971.00	838.117
283.15	62025.00	852.74
283.15	267.60	817.937
283.15	2020.20	819.134
283.15	7034.80	822.538
283.15	9991.90	824.485
283.15	15011.00	827.609
283.15	25044.00	833.615
283.15	28046.00	835.368
283.15	32970.00	838.092
283.15	34960.00	839.141
283.15	37943.00	840.737
283.15	44940.00	844.325
283.15	49996.00	846.902
283.15	51982.00	847.942
283.15	57949.00	850.826
283.15	991.30	818.415
283.15	2914.80	819.722
283.15	4946.50	821.145
283.15	9021.60	823.807
283.15	34017.00	838.557
283.15	40004.00	841.811
283.15	42058.00	842.896
283.15	54965.00	849.358
283.15	64998.00	854.215
283.15	878.60	818.388
283.15	20045.00	830.642
283.15	30052.00	836.501
283.15	48022.00	845.954
283.15	59996.00	851.847
283.15	22057.00	831.928
283.16	65971.00	854.69
283.16	101.20	817.825
288.15	882.70	814.204
288.15	2917.80	815.651
288.15	9018.60	819.847
288.15	10040.00	820.583
288.15	20693.00	827.38
288.15	32084.00	834.074
288.15	37993.00	837.311
288.15	40041.00	838.449
288.15	44979.00	841.064
288.15	52032.00	844.696
288.15	55077.00	846.251
288.15	61974.00	849.542
288.15	64942.00	850.93
288.15	391.30	813.84
288.15	66025.00	851.488
288.15	7088.80	818.541
288.15	12072.00	821.91
288.15	17968.00	825.72
288.15	78.50	813.612
288.15	25002.00	829.984
288.15	28026.00	831.832
288.15	30035.00	832.896
288.15	33050.00	834.714
288.15	34036.00	835.152
288.15	50068.00	843.734
288.15	554.40	813.953
288.15	2057.50	815.033
288.15	5041.40	817.16
288.15	15001.00	823.877
288.15	20068.00	826.976
288.15	22020.00	828.211
288.15	35077.00	835.674
288.15	42023.00	839.459
288.15	989.10	814.282
288.15	48045.00	842.655
288.15	58004.00	847.666
288.15	59988.00	848.618
293.15	33151.00	832.036
293.15	28066.00	829.163
293.15	58072.00	845.282
293.15	825.10	811.053
293.15	66045.00	849.224
293.15	21987.00	825.417
293.15	27986.00	829.06
293.15	35000.00	833.078
293.15	45068.00	838.658
293.15	1971.70	811.916
293.15	3060.60	812.72
293.15	5011.00	814.074
293.15	9042.10	816.992
293.15	91.10	810.528
293.15	10036.00	817.626
293.15	11947.00	818.963
293.15	14941.00	820.924
293.15	34099.00	832.526
293.15	40081.00	835.959
293.15	42099.00	837.008
293.15	54966.00	843.81
293.16	1045.20	811.221
293.16	7096.80	815.616
293.16	17889.00	822.832
293.16	19992.00	824.147
293.16	24983.00	827.251
293.16	29976.00	830.11
293.16	32232.00	831.521
293.16	476.40	810.81
293.16	38027.00	834.783
293.16	48022.00	840.192
293.16	50085.00	841.31
293.16	52032.00	842.308
293.16	60018.00	846.257
293.16	64991.00	848.649
293.16	305.20	810.686
293.16	61962.00	847.209
298.15	33113.00	828.365
298.15	45021.00	835.052
298.15	55016.00	840.375
298.15	65018.00	845.412
298.15	10107.00	813.67
298.15	38097.00	831.213
298.15	40161.00	832.357
298.15	57931.00	841.819
298.15	59914.00	842.826
298.15	22004.00	821.641
298.15	50068.00	837.797
298.15	62036.00	843.934
298.15	5067.60	810.04
298.15	305.40	806.45
298.15	42029.00	833.462
298.15	1980.90	807.747
298.15	48107.00	836.745
298.15	3167.80	808.637
298.15	7065.30	811.55
298.15	854.50	806.874
298.15	20128.00	820.445
298.15	25081.00	823.55
298.15	33924.00	828.845
298.15	98.10	806.282
298.15	42359.00	833.614
298.16	9120.90	813.012
298.16	11970.00	814.957
298.16	15220.00	817.234
298.16	17984.00	819.076
298.16	28040.00	825.42
298.16	30089.00	826.686
298.16	32030.00	827.814
298.16	35217.00	829.575
298.16	52020.00	838.835
298.16	493.70	806.599
298.16	1012.60	806.992
298.16	66118.00	845.919
303.15	498.90	802.435
303.15	32862.00	824.267
303.15	34081.00	824.9
303.15	39904.00	828.27
303.15	1977.60	803.554
303.15	52073.00	834.942
303.15	55075.00	836.525
303.15	57989.00	838.099
303.15	64988.00	841.599
303.15	33112.00	824.372
303.15	304.10	802.278
303.15	62052.00	840.165
303.15	4930.40	805.792
303.15	42014.00	829.398
303.15	44896.00	831.035
303.15	50065.00	833.864
303.15	979.10	802.787
303.15	19974.00	816.207
303.15	21920.00	817.555
303.15	31958.00	823.711
303.15	34980.00	825.355
303.15	59979.00	839.13
303.15	66030.00	842.119
303.15	11975.00	810.901
303.15	900.60	802.733
303.15	15044.00	812.956
303.15	24992.00	819.44
303.15	37951.00	827.164
303.15	47951.00	832.781
303.16	10014.00	809.449
303.16	18021.00	814.973
303.16	27933.00	821.256
303.16	29990.00	822.537
303.16	8858.20	808.638
303.16	2964.90	804.3
303.16	100.00	802.125
303.16	7045.60	807.335
308.15	12009.00	807.267
308.15	803.30	798.75
308.15	17850.00	811.315
308.15	21988.00	814.131
308.15	27955.00	817.999
308.15	32886.00	820.911
308.15	1916.70	799.642
308.15	4990.20	802.048
308.15	2980.70	800.489
308.15	19930.00	812.759
308.15	25012.00	816.144
308.15	31929.00	820.41
308.15	32941.00	821.059
308.15	37971.00	823.987
308.15	54982.00	833.542
308.15	9863.10	805.692
308.15	40011.00	825.154
308.15	8864.30	804.962
308.15	494.10	798.504
308.15	58009.00	835.036
308.15	1039.50	798.954
308.15	29906.00	819.191
308.15	34011.00	821.636
308.15	45017.00	828.081
308.15	50044.00	830.856
308.15	61985.00	837.136
308.15	64981.00	838.691
308.15	41998.00	826.392
308.15	48033.00	829.748
308.15	51977.00	831.933
308.15	6964.90	803.548
308.15	274.30	798.317
308.15	60030.00	836.098
308.16	15069.00	809.4
308.16	34949.00	822.224
308.16	85.20	798.155
308.16	66088.00	839.237
313.15	17921.00	807.72
313.15	24862.00	812.41
313.15	15059.00	805.716
313.15	19932.00	809.082
313.15	10209.00	802.164
313.15	6921.80	799.704
313.15	12020.00	803.525
313.15	5111.80	798.292
313.15	27869.00	814.438
313.15	29957.00	815.731
313.15	54924.00	830.321
313.15	32980.00	817.674
313.15	33981.00	818.214
313.15	2109.70	795.902
313.15	41978.00	822.973
313.15	59932.00	832.96
313.15	1088.80	795.074
313.15	32107.00	817.091
313.15	33002.00	817.783
313.15	38127.00	820.76
313.15	47880.00	826.39
313.15	103.10	794.254
313.15	52097.00	828.677
313.15	62004.00	834.048
313.15	66113.00	836.222
313.15	22058.00	810.55
313.15	316.00	794.433
313.15	9210.70	801.445
313.15	35045.00	818.819
313.15	44946.00	824.676
313.15	3137.00	796.707
313.15	58082.00	831.994
313.15	569.60	794.643
313.15	64954.00	835.652
313.16	860.70	794.888
313.16	39997.00	821.817
313.16	50021.00	827.556
318.15	11896.00	799.896
318.15	66028.00	833.327
318.15	33016.00	814.458
318.15	37838.00	817.415
318.15	59923.00	830.12
318.15	2933.20	792.866
318.15	8989.00	797.678
318.15	44884.00	821.648
318.15	72.70	790.456
318.15	18102.00	804.461
318.15	47944.00	823.402
318.15	150.10	790.516
318.15	57972.00	829.016
318.15	336.30	790.675
318.15	22094.00	807.257
318.15	29998.00	812.541
318.15	19985.00	805.78
318.15	40093.00	818.817
318.15	1105.70	791.334
318.15	54944.00	827.433
318.15	10075.00	798.523
318.15	1929.10	792.026
318.15	65022.00	832.785
318.16	27909.00	811.139
318.16	31957.00	813.824
318.16	891.00	791.16
318.16	34110.00	815.009
318.16	35048.00	815.63
318.16	6926.70	796.098
318.16	41996.00	819.89
318.16	5020.80	794.556
318.16	49950.00	824.565
318.16	14800.00	802.072
318.16	52037.00	825.741
318.16	61930.00	831.241
318.16	24873.00	809.191
318.16	590.90	790.894
323.15	296.10	786.326
323.15	49934.00	820.799
323.15	58045.00	825.293
323.15	17981.00	800.333
323.15	2006.90	787.814
323.15	54964.00	823.594
323.15	60050.00	826.448
323.15	64999.00	829.093
323.15	35113.00	811.773
323.15	9029.90	793.564
323.15	2966.60	788.632
323.15	48025.00	819.642
323.15	95.00	786.145
323.15	52114.00	821.994
323.15	20038.00	801.815
323.15	4996.20	790.328
323.15	34081.00	811.155
323.15	24993.00	805.264
323.15	7042.10	792.001
323.15	15111.00	798.229
323.15	62131.00	827.565
323.15	32079.00	809.955
323.15	37953.00	813.623
323.15	528.40	786.535
323.15	10090.00	794.392
323.15	42011.00	816.075
323.15	21995.00	803.198
323.15	994.20	786.944
323.15	11914.00	795.8
323.16	30055.00	808.674
323.16	27958.00	807.28
323.16	33067.00	810.61
323.16	40047.00	814.861
323.16	44937.00	817.856
323.16	920.70	786.888
323.16	66131.00	829.687
328.15	33066.00	807.772
328.15	35030.00	808.989
328.15	38010.00	810.915
328.15	44953.00	815.144
328.15	47978.00	816.959
328.15	49927.00	818.128
328.15	54947.00	821.045
328.15	59991.00	823.77
328.15	27979.00	804.324
328.15	61982.00	824.89
328.15	65032.00	826.439
328.15	66046.00	826.965
328.15	5013.40	786.446
328.15	2996.70	784.66
328.15	24924.00	802.164
328.15	57939.00	822.658
328.15	994.10	782.825
328.15	39969.00	812.181
328.15	34013.00	808.285
328.15	41959.00	813.311
328.15	289.90	782.179
328.15	51997.00	819.32
328.15	32060.00	807.104
328.15	29958.00	805.68
328.15	33107.00	807.703
328.15	9017.00	789.881
328.15	97.90	781.987
328.15	10040.00	790.727
328.15	897.50	782.733
328.15	6974.90	788.15
328.15	1988.80	783.741
328.16	20279.00	798.799
328.16	12210.00	792.522
328.16	18061.00	797.122
328.16	22013.00	800.057
328.16	15055.00	794.783
328.16	501.00	782.371
333.15	34086.00	805.827
333.15	37894.00	808.332
333.15	4997.40	783.921
333.15	47936.00	814.509
333.15	51953.00	816.927
333.15	58057.00	820.5
333.15	32067.00	804.524
333.15	62049.00	822.689
333.15	35075.00	806.492
333.15	40111.00	809.759
333.15	30016.00	803.156
333.15	22034.00	797.567
333.15	66005.00	824.853
333.15	44974.00	812.823
333.15	45490.00	813.093
333.15	49920.00	815.727
333.15	54876.00	818.691
333.15	7002.40	785.686
333.15	59993.00	821.547
333.15	64970.00	824.293
333.15	10210.00	788.367
333.15	41947.00	810.938
333.15	9032.00	787.401
333.15	532.60	779.903
333.15	28040.00	801.782
333.15	1987.20	781.249
333.15	897.80	780.245
333.15	3023.40	782.177
333.15	15008.00	792.251
333.16	303.50	779.691
333.16	25027.00	799.667
333.16	12011.00	789.847
333.16	20036.00	796.123
333.16	1003.00	780.346
333.16	17992.00	794.568
333.16	87.70	779.482
333.16	33073.00	805.134
338.15	25026.00	796.362
338.15	22041.00	794.077
338.15	14885.00	788.349
338.15	35012.00	803.345
338.15	52127.00	814.375
338.15	60014.00	819.058
338.15	65012.00	821.872
338.15	66057.00	822.451
338.15	47971.00	811.881
338.15	57940.00	817.865
338.15	32882.00	801.907
338.15	10034.00	784.276
338.15	44978.00	809.926
338.15	19927.00	792.473
338.15	49999.00	813.099
338.15	898.50	775.911
338.15	41990.00	808.025
338.15	5018.60	779.821
338.15	309.80	775.333
338.15	2936.10	777.859
338.15	29994.00	799.911
338.15	39987.00	806.717
338.15	17956.00	790.925
338.15	80.90	775.106
338.15	33937.00	802.603
338.15	561.60	775.578
338.15	1014.10	776.019
338.16	2000.20	776.987
338.16	6917.30	781.55
338.16	11959.00	785.981
338.16	27976.00	798.446
338.16	54992.00	816.085
338.16	31949.00	801.318
338.16	62074.00	820.252
338.16	37962.00	805.345
338.16	9046.90	783.457
338.16	67534.00	823.221
343.15	1017.70	770.563
343.15	52026.00	808.534
343.15	4994.80	774.313
343.15	30082.00	794.441
343.15	297.30	769.853
343.15	911.70	770.459
343.15	65070.00	815.911
343.15	44927.00	804.186
343.15	33097.00	796.546
343.15	520.30	770.07
343.15	2332.50	771.83
343.15	2968.30	772.434
343.15	61967.00	814.212
343.15	10060.00	778.847
343.15	6976.60	776.117
343.15	47908.00	806.033
343.15	1994.60	771.497
343.15	73.70	769.631
343.15	12025.00	780.506
343.15	59944.00	813.181
343.15	19985.00	786.983
343.15	66059.00	816.518
343.15	17975.00	785.398
343.15	9002.60	777.941
343.15	28045.00	793.012
343.15	40012.00	801.058
343.15	25091.00	790.858
343.15	14928.00	782.929
343.15	35030.00	797.771
343.15	50059.00	807.349
343.15	22033.00	788.56
343.15	32170.00	795.891
343.15	41972.00	802.307
343.15	37943.00	799.701
343.16	34034.00	797.101
343.16	54919.00	810.24
343.16	57986.00	812.021
348.15	49950.00	804.611
348.15	88.80	765.578
348.15	3051.10	768.513
348.15	859.80	766.355
348.15	64942.00	813.608
348.15	5094.00	770.529
348.15	40026.00	798.192
348.15	47915.00	803.304
348.15	22163.00	785.27
348.15	66153.00	814.319
348.15	1974.90	767.461
348.15	35045.00	794.751
348.15	57945.00	809.531
348.15	52167.00	805.991
348.15	20111.00	783.649
348.15	55022.00	807.759
348.15	33959.00	793.985
348.15	30149.00	791.333
348.15	32161.00	792.797
348.15	462.20	765.945
348.15	14792.00	779.258
348.15	974.20	766.465
348.15	37937.00	796.729
348.15	10025.00	775.087
348.15	60030.00	810.761
348.15	42066.00	799.57
348.15	28080.00	789.8
348.16	7050.20	772.352
348.16	45051.00	801.465
348.16	32942.00	793.364
348.16	9003.20	774.145
348.16	291.70	765.77
348.16	62063.00	811.961
348.16	17899.00	781.843
348.16	25100.00	787.55
348.16	12187.00	777.001
353.15	21894.00	781.405
353.15	4963.90	766.051
353.15	17977.00	778.173
353.15	336.00	761.273
353.15	40143.00	795.172
353.15	19937.00	779.792
353.15	29936.00	787.797
353.15	12128.00	772.98
353.15	52082.00	803.184
353.15	10005.00	771.015
353.15	45002.00	798.55
353.15	48029.00	800.525
353.15	926.00	761.914
353.15	7000.90	768.126
353.15	32961.00	790.048
353.15	37913.00	793.571
353.15	1016.40	762.008
353.15	50145.00	801.944
353.15	34945.00	791.423
353.15	60098.00	808.146
353.15	14954.00	775.544
353.15	42067.00	796.559
353.15	65063.00	811.071
353.15	2992.10	764.106
353.15	31876.00	789.263
353.15	86.20	760.995
353.15	24908.00	783.869
353.15	27850.00	786.199
353.15	9062.30	770.136
353.15	57980.00	806.879
353.15	55132.00	805.077
353.15	572.60	761.533
353.16	2113.40	763.181
353.16	62043.00	809.275
353.16	33964.00	790.701
353.16	66024.00	811.636
358.15	60043.00	804.453
358.15	17041.00	772.871
358.15	32793.00	786.01
358.15	50038.00	798.154
358.15	926.80	756.64
358.15	31978.00	785.37
358.15	4930.00	760.98
358.15	52081.00	799.474
358.15	37872.00	789.731
358.15	55073.00	801.393
358.15	62067.00	805.674
358.15	28035.00	782.278
358.15	33850.00	786.716
358.15	17965.00	773.738
358.15	66109.00	808.067
358.15	47958.00	796.761
358.15	40037.00	791.31
358.15	35027.00	787.554
358.15	64986.00	807.407
358.15	22175.00	777.415
358.15	14905.00	770.903
358.15	1013.90	756.732
358.15	12137.00	768.259
358.15	42100.00	792.749
358.15	25059.00	779.849
358.15	3021.20	758.947
358.15	508.40	756.19
358.15	57918.00	803.161
358.15	10073.00	766.29
358.15	264.10	755.935
358.15	30002.00	783.844
358.16	2083.90	757.886
358.16	95.10	755.754
358.16	45054.00	794.81
358.16	9030.20	765.202
358.16	20162.00	775.665
358.16	6993.50	763.142
363.15	50050.00	794.458
363.15	34000.00	783.178
363.15	54940.00	797.589
363.15	37919.00	786.081
363.15	31961.00	781.745
363.15	4979.20	757.84
363.15	11971.00	764.806
363.15	47947.00	793.03
363.15	27993.00	778.673
363.15	94.00	752.456
363.15	35028.00	783.945
363.15	42016.00	788.986
363.15	59980.00	800.724
363.15	30062.00	780.285
363.15	17973.00	770.255
363.15	33033.00	782.563
363.15	57917.00	799.479
363.15	601.70	753.061
363.15	892.90	753.404
363.15	19940.00	771.991
363.15	39916.00	787.488
363.15	52023.00	795.718
363.15	334.00	752.741
363.15	2940.40	755.648
363.15	961.60	753.487
363.15	1986.00	754.594
363.15	64924.00	803.734
363.15	66088.00	804.418
363.15	1034.70	753.567
363.15	9959.50	762.855
363.15	62043.00	802.008
363.15	14936.00	767.534
363.15	24872.00	776.146
363.16	8964.80	761.886
363.16	21933.00	773.696
363.16	44987.00	791.029
363.16	6920.20	759.821
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
313.08	1006.00	795.22
313.08	2017.00	796.08
313.08	3007.00	796.85
313.08	4010.00	797.64
313.08	5016.00	798.44
313.08	6017.00	799.22
313.08	7011.00	800.0
313.08	8006.00	800.77
313.08	9019.00	801.53
313.08	10008.00	802.27
313.08	11014.00	803.01
313.08	12016.00	803.73
313.08	13016.00	804.46
313.08	14013.00	805.18
313.08	15010.00	805.91
313.08	16003.00	806.58
313.08	16999.00	807.29
313.08	17999.00	807.98
313.08	19024.00	808.67
313.08	20005.00	809.33
313.08	21013.00	810.09
313.08	22003.00	810.75
313.08	23024.00	811.41
313.08	24027.00	812.09
313.08	24234.00	812.21
323.05	999.00	787.38
323.05	2026.00	788.22
323.05	3007.00	789.03
323.05	4024.00	789.91
323.05	5012.00	790.75
323.05	6016.00	791.57
323.05	7023.00	792.4
323.05	8004.00	793.16
323.05	9009.00	793.98
323.05	10007.00	794.78
323.05	11004.00	795.57
323.05	11995.00	796.32
323.05	13007.00	797.09
323.05	14022.00	797.85
323.05	14989.00	798.63
323.05	16006.00	799.33
323.05	16998.00	800.1
323.05	18001.00	800.84
323.05	19025.00	801.56
323.05	19993.00	802.28
323.05	21032.00	803.06
323.05	22006.00	803.74
323.05	22993.00	804.41
323.05	24012.00	805.16
323.05	24418.00	805.43
332.93	1013.00	779.33
332.93	2026.00	780.27
332.93	3014.00	781.21
332.93	4006.00	782.04
332.93	5000.00	782.91
332.93	6013.00	783.78
332.93	6997.00	784.6
332.93	8003.00	785.5
332.93	9005.00	786.32
332.93	10001.00	787.17
332.93	10996.00	787.97
332.93	12003.00	788.8
332.93	12993.00	789.62
332.93	14001.00	790.38
332.93	15016.00	791.22
332.93	15998.00	791.96
332.93	16999.00	792.72
332.93	18009.00	793.53
332.93	18986.00	794.29
332.93	20043.00	795.08
332.93	21056.00	795.87
332.93	22040.00	796.59
332.93	23009.00	797.3
332.93	24001.00	798.04
332.93	24515.00	798.46
342.86	1026.00	770.92
342.86	2007.00	771.87
342.86	3003.00	772.85
342.86	4051.00	773.84
342.86	5008.00	774.72
342.86	6023.00	775.59
342.86	7010.00	776.55
342.86	8000.00	777.42
342.86	9001.00	778.28
342.86	10005.00	779.2
342.86	11006.00	780.06
342.86	12010.00	780.9
342.86	13033.00	781.77
342.86	14017.00	782.62
342.86	15001.00	783.45
342.86	16009.00	784.29
342.86	17016.00	785.14
342.86	17991.00	785.93
342.86	19023.00	786.79
342.86	19999.00	787.57
342.86	21000.00	788.37
342.86	22003.00	789.15
342.86	22989.00	789.91
342.86	24004.00	790.69
342.86	24621.00	791.2
352.79	1020.00	762.66
352.79	2014.00	763.68
352.79	3007.00	764.68
352.79	3998.00	765.67
352.79	4998.00	766.69
352.79	5997.00	767.68
352.79	7006.00	768.64
352.79	8005.00	769.61
352.79	9007.00	770.53
352.79	9997.00	771.44
352.79	11008.00	772.38
352.79	12000.00	773.26
352.79	13043.00	774.22
352.79	14002.00	775.11
352.79	15000.00	775.98
352.79	16000.00	776.85
352.79	16992.00	777.72
352.79	17988.00	778.56
352.79	18994.00	779.41
352.79	20012.00	780.22
352.79	21003.00	781.04
352.79	22010.00	781.87
352.79	22971.00	782.68
352.79	24021.00	783.49
352.79	24573.00	783.95
362.67	1043.00	753.5
362.67	2116.00	754.77
362.67	3026.00	755.74
362.67	4013.00	756.82
362.67	5024.00	757.87
362.67	6047.00	758.93
362.67	7014.00	759.93
362.67	8012.00	760.98
362.67	9025.00	762.03
362.67	10015.00	762.94
362.67	11002.00	763.92
362.67	12002.00	764.89
362.67	13011.00	765.86
362.67	14011.00	766.84
362.67	15014.00	767.7
362.67	16006.00	768.67
362.67	17009.00	769.58
362.67	18008.00	770.48
362.67	18993.00	771.37
362.67	19990.00	772.21
362.67	21007.00	773.1
362.67	21997.00	773.96
362.67	23014.00	774.89
362.67	24000.00	775.58
362.67	24563.00	776.12
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	108.00	1399.203
253.15	5065.00	1423.053
253.15	10086.00	1446.233
253.15	15035.00	1468.319
253.15	20115.00	1490.177
253.15	25062.00	1510.75
253.15	30526.00	1532.696
273.15	103.00	1326.117
273.15	5008.00	1351.87
273.15	10094.00	1377.167
273.15	15185.00	1401.443
273.15	20115.00	1424.124
273.15	25088.00	1446.132
273.15	30170.00	1467.891
293.15	104.00	1256.423
293.15	5067.00	1284.566
293.15	10144.00	1311.663
293.15	15081.00	1336.897
293.15	20094.00	1361.485
293.15	25087.00	1384.998
293.15	30176.00	1408.068
313.15	100.00	1189.161
313.15	5050.00	1219.204
313.15	10082.00	1248.164
313.15	15167.00	1275.967
313.15	20187.00	1302.165
313.15	25473.00	1328.5
313.15	30162.00	1351.047
333.15	99.00	1122.893
333.15	5055.00	1155.491
333.15	10099.00	1186.761
333.15	15058.00	1215.841
333.15	20149.00	1244.214
333.15	25167.00	1270.825
333.15	30276.00	1296.753
353.15	100.00	1056.353
353.15	5013.00	1091.582
353.15	10032.00	1125.304
353.15	15066.00	1157.065
353.15	20085.00	1186.968
353.15	25075.00	1215.14
353.15	30204.00	1242.721
Reference

Operational condition: Frequency, MHz = 8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Speed of sound, m/s - Liquid
250.00	67.00	1411.8
218.17	100.00	1536.6
249.99	100.00	1412.0
300.04	101.00	1234.1
350.11	104.00	1067.1
400.14	145.00	891.2
449.96	576.00	696.4
350.11	911.00	1073.1
400.14	933.00	898.8
300.03	1100.00	1240.0
218.25	1111.00	1540.5
449.96	1176.00	704.8
499.96	1636.00	472.8
400.14	1839.00	907.3
449.96	2010.00	716.0
249.99	2060.00	1421.4
350.11	2067.00	1081.4
218.26	2129.00	1544.8
300.03	2196.00	1246.4
499.96	2336.00	490.0
350.11	4569.00	1099.0
400.14	4864.00	934.6
499.96	4923.00	544.0
249.99	5075.00	1435.7
300.03	5369.00	1264.5
218.31	5399.00	1558.2
499.96	7243.00	586.7
249.98	9057.00	1453.9
350.11	9077.00	1129.2
400.12	9483.00	973.3
449.96	9527.00	803.9
218.28	9570.00	1575.2
300.03	9681.00	1288.1
499.96	9870.00	626.9
499.95	19314.00	741.4
218.22	19695.00	1614.9
300.03	20060.00	1341.4
350.11	20660.00	1199.6
400.14	20722.00	1055.9
449.96	21165.00	910.4
249.98	22437.00	1511.7
499.91	25968.00	806.2
400.14	36029.00	1150.7
217.92	39005.00	1685.4
449.96	39912.00	1043.3
300.03	40032.00	1432.5
499.95	40048.00	918.1
250.01	40124.00	1581.1
350.10	40651.00	1303.9
249.98	58985.00	1648.4
400.14	59027.00	1269.1
300.02	59057.00	1509.0
350.10	59555.00	1388.7
218.12	59881.00	1753.2
449.96	59899.00	1156.8
499.96	60162.00	1045.7
400.14	79223.00	1357.8
249.98	79282.00	1714.5
300.02	79463.00	1582.8
449.96	79678.00	1251.8
218.18	79839.00	1813.2
499.96	80004.00	1149.3
350.09	80590.00	1472.2
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.63]	kPa	[303.83; 411.84]	The Yaw...
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.47969e+01
Coefficient B			-2.95887e+03
Coefficient C			-9.99030e+01
Temperature range, min.			303.83
Temperature range, max.			411.84
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400
Pvap	1.33	kPa	303.83	Calculated Property
Pvap	2.99	kPa	315.83	Calculated Property
Pvap	6.14	kPa	327.83	Calculated Property
Pvap	11.76	kPa	339.83	Calculated Property
Pvap	21.16	kPa	351.83	Calculated Property
Pvap	36.10	kPa	363.84	Calculated Property
Pvap	58.78	kPa	375.84	Calculated Property
Pvap	91.90	kPa	387.84	Calculated Property
Pvap	138.64	kPa	399.84	Calculated Property
Pvap	202.63	kPa	411.84	Calculated Property
Pvap	[5.55e-07; 4329.98]	kPa	[183.85; 563.00]	KDB Vap...
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			8.67221e+01
Coefficient B			-9.12750e+03
Coefficient C			-9.88261e+00
Coefficient D			1.42848e-06
Temperature range, min.			183.85
Temperature range, max.			563.00
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 200 300 400 500
Pvap	5.55e-07	kPa	183.85	Calculated Property
Pvap	7.74e-04	kPa	225.98	Calculated Property
Pvap	0.08	kPa	268.11	Calculated Property
Pvap	2.09	kPa	310.23	Calculated Property
Pvap	20.85	kPa	352.36	Calculated Property
Pvap	113.60	kPa	394.49	Calculated Property
Pvap	408.48	kPa	436.62	Calculated Property
Pvap	1093.12	kPa	478.74	Calculated Property
Pvap	2357.78	kPa	520.87	Calculated Property
Pvap	4329.98	kPa	563.00	Calculated Property

Similar Compounds

Find more compounds similar to 1-Butanol.

Mixtures

• Isopropyl Alcohol + 1-Butanol
• 1-Butanol + Dimethyl Sulfoxide
• p-Xylene + 1-Butanol
• Trichloromethane + 1-Butanol
• Benzene + 1-Butanol
• Benzene + Trichloromethane + 1-Butanol
• n-Hexane + 1-Butanol
• 1-Butanol + Cyclohexane
• Tetraglyme + 1-Butanol
• 1-Butanol + Acetic acid, methyl ester
• 1-Butanol + Ethyl Acetate
• 1-Butanol + Ethanol, 2,2'-oxybis-
• 1-Butanol + Water
• 1-Butanol + Butyl lactate
• Piperazine, 1-methyl- + 1-Butanol
• Triethylamine + 1-Butanol
• n-Hexane + Triethylamine + 1-Butanol
• 1,3-Dioxolane + 1-Butanol + Water
• Phenol, 2-methyl- + 1-Butanol
• p-Cresol + 1-Butanol

Find more mixtures with 1-Butanol.

Sources

• KDB Pure (Korean Thermophysical Properties Databank)
• KDB Vapor Pressure Data
• Crippen Method
• Dortmund Data Bank Vapor-Liquid Equilibrium Data
• Speeds of Sound and Isentropic Compressibilities in Binary Mixtures of 2-Propanol with Several 1-Alkanols at 298.15K
• Measurements of the Properties of Binary Mixtures of Dimethylsulphoxide (DMSO) with 1-Alkanols (C4, C6, C7) at 303.15K
• Isobaric Vapor Liquid Equilibria of 1-Butanol p-Xylene System1
• Temperature Dependence of Densities and Excess Molar Volumes of the Ternary Mixture (1-Butanol + Chloroform + Benzene) and its Binary Constituents (1-Butanol + Chloroform and 1-Butanol + Benzene)
• Acoustic and Thermophysical Properties of Binary Liquid Mixtures of Primary Butanols with Hexane and Cyclohexane at 293.15 K
• Volumetric Properties, Viscosities, and Refractive Indices of the Binary Systems 1-Butanol + PEG 200, + PEG 400, and + TEGDME
• 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
• Densities, Ultrasonic Speeds, and Excess Properties of Binary Mixtures of Diethylene Glycol with 1-Butanol, 2-Butanol, and 1,4-Butanediol at Different Temperatures
• Revision of the volumetric method for measurements of liquid liquid equilibria in binary systems
• Vapor liquid equilibria and excess volumes of the binary systems ethanol + ethyl lactate, isopropanol + isopropyl lactate and n-butanol + n-butyl lactate at 101.325 kPa
• Isobaric vapor liquid phase equilibria for the binary systems of tert-butanol + 2-ethyl-1-hexanol and n-butanol + 2-ethyl-1-hexanol
• 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
• Salt effect on vapor liquid equilibria for binary systems of propanol/CaCl2 and butanol/CaCl2
• Excess molar volumes and excess molar enthalpies of binary and ternary mixtures of (ethanol or 1-butanol), triethylamine and n-hexane
• Measurement of infinite dilution activity coefficients of 1-alkanols (C1 C5) in water as a function of temperature (273 373 K)
• The co-solubility of 2-ethylhexanoic acid and some liquid alcohols in supercritical carbon dioxide
• 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
• 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
• Phase behaviour of I-hexyloxymethyl-3-methyl-imidazolium and 1,3-dihexyloxymethyl-imidazolium based ionic liquids with alcohols, water, ketones and hydrocarbons: The effect of cation and anion on solubility
• Liquid liquid equilibrium of ternary systems containing nicotine
• Vapour liquid equilibrium for the systems butane + methanol, +2-propanol, +1-butanol, +2-butanol, +2-methyl-2-propanol at 364.5K
• 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
• Determination of partial molar excess enthalpies at infinite dilution for the systems four alcohols + [bmim]PF6 at different temperatures by isothermal titration calorimeter
• Liquid liquid equilibria of water + 1-butanol + methyl methacrylate or butyl methacrylate or isobutyl methacrylate at 288.15K and 318.15K
• High-pressure phase equilibrium for ethylene + 1-butanol at 283.65 K and 290.80 K
• 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
• Vapor liquid equilibria for the binary mixtures of 2,3-butanediol with n-butanol, n-butyl acetate, and ethyl acetate at 101.3 kPa
• 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
• Measurement and correlation of binary vapor liquid equilibria of isomeric butanols with 1,4-dioxane
• Liquid liquid equilibria of water + 2,3-butanediol + 1-butanol at T = 298.15 K, T = 308.15K and T = 318.15K
• Molecular interactions in binary mixtures of formamide with 1-butanol, 2-butanol, 1,3-butanediol and 1,4-butanediol at different temperatures: An ultrasonic and viscometric study
• Determination and correlation of molar excess enthalpies of binary systems 2,4-pentanedione + (1-butanol, + 2-methyl-1-propanol, + 1-pentanol, + 1-heptane, + ethyl acetate, and + water)
• Vapour liquid equilibria, azeotropic data, excess enthalpies, activity coefficients at infinite dilution and solid liquid equilibria for binary alcohol ketone systems
• 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
• Solubility of antioxidant 1010 in pure alkanols
• Isobaric vapour liquid equilibria for the binary systems 4-methyl-2-pentanone + 1-butanol and + 2-butanol at 20 and 101.3 kPa
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium trifluoromethanesulfonate using GLC
• 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
• Binary, ternary and quaternary liquid liquid equilibria in 1-butanol, oleic acid, water and n-heptane mixtures
• Excess enthalpies of ether + alcohol + hydrocarbon mixtures: Binary and ternary mixtures containing dibutyl ether (DBE), 1-butanol and benzene at 298.15K and 313.15K
• 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
• Experimental solid-liquid phase equilibria of {cholesterol + binary solvent mixture: 1-Alcohol (C4-C10) + cyclohexane}
• Excess enthalpies of oxygenated compounds + hydrocarbon mixtures: Binary and ternary mixtures containing dibutyl ether (DBE), 1-butanol and 2,2,4-trimethylpentane at 298.15 K
• Excess molar enthalpies of diethyl malonate+ (1-butanol, 2-methyl-1-propanol, 1-pentanol, n-heptane, and ethyl acetate) at T= (288.2, 298.2, 313.2, 328.2, 338.2, and 348.2 K) and p = 101.3 kPa
• Measurement and prediction of multicomponent diffusion coefficients in four ternary liquid systems
• (Solid + liquid) and (liquid + liquid) phase equilibria study and correlation of the binary systems {N-butyl-3-methylpyridinium tosylate + water, or + an alcohol, or + a hydrocarbon}
• Solubility of CF4 in lower alcohols
• High-pressure phase behavior of ternary systems (carbon dioxide + alkanol + hydrophobic ionic liquid)
• Vapor-liquid equilibria and phase densities at saturation of carbon dioxide + 1-butanol and carbon dioxide + 2-butanol from 313 to 363 K
• Isobaric vapor-liquid equilibria for water + n-propanol + n-butanol ternary system at atmospheric pressure
• 1-Butanol + hexylamine + n-heptane at temperature range (288.15 323.15 K): Experimental density data, excess molar volumes determination and modeling with cubic EOS
• Experimental and predicted excess molar enthalpies of binary mixtures containing 2,2'-oxybis[propane], benzene, butan-1-ol, 2-methylpropan-1-ol, 2-methyl-2-ene-1-propanol at 303.15 K
• Experimental and theoretical study on liquid-liquid equilibrium of 1-butanol + water + NaNO3 at 25 and 35 deg C
• Liquid density of 1-butanol at pressures up to 140MPa and from 293.15K to 403.15K
• Solubility of HFCs in lower alcohols
• VLE of CO2 + glycerol + (ethanol or 1-propanol or 1-butanol)
• Thermophysical properties of pure 1-ethyl-3-methylimidazolium methylsulfate and its binary mixtures with alcohols
• Experimental measurement and modeling of solubility of LiBr and LiNO3 in methanol, ethanol, 1-propanol, 2-propanol and 1-butanol
• 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
• Ether + alcohol + hydrocarbon mixtures in fuels and bio-fuels: Excess enthalpies of binary mixtures containing dibutyl ether (DBE) or 1-butanol and 1-hexene or methylcyclohexane or toluene or cyclohexane or 2,2,4-trimethylpentane at 298.15K and 313.15K
• LLE, VLE and VLLE data for the water n-butanol n-hexane system at atmospheric pressure
• Solubility of caprolactam in different organic solvents
• Liquid-liquid equilibria of aqueous systems containing alcohol and ammonium sulfate
• Measurements and correlation of liquid-liquid equilibria of 4-methyl-2-pentanone + ethanol + water and 4-methyl-2-pentanone + n-butanol + water ternary systems between 283.2 and 323.2 K
• Experimental and theoretical study on liquid liquid equilibrium of 1-butanol + water + NH4Cl at 298.15, 308.15 and 318.15 K
• 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
• 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
• Experimental and calculated liquid-liquid equilibrium data for water + furfural + solvents
• Liquid-liquid equilibrium for the ternary system of 1-butanol + 3-methyl-1-butanol + water at different temperatures
• Experimental study of the PVT and CVVT properties of n-butanol in the critical region
• Prediction of different thermodynamic properties for systems of alcohols and sulfate-based anion Ionic Liquids using modified UNIFAC
• Investigation on vapor liquid equilibrium for 2-propanol + 1-butanol + 1-pentanol at 101.3 kPa
• Phase behaviour of ionic liquid 1-butyl-1-methylpyrrolidinium tris(pentafluoroethyl)trifluorophosphate with alcohols, water and aromatic hydrocarbons
• The liquid-liquid coexistence curves of {x 1-octyl-3-methylimidazolium hexafluorophosphate + (1-x) 1-butanol} and {x 1-octyl-3-methylimidazolium hexafluorophosphate + (1 - x) 2-butanol} in the critical region
• Thermodynamics of solubility of thiomalic acid in different organicsolvents from 278.15 K to 333.15 K
• Isobaric VLE data for the system of butan-1-ol + butylethanoate + 1-butyl-3-methylimidazoliumbis[(trifluoromethyl)sulfonyl]imide
• The effect of temperature on the liquid-liquid equilibria of somealiphatic alcohols + di-sodium hydrogen citrate + water systems: Experimental and correlation
• Liquid-liquid equilibrium data for systems containing of formic acid, water, and primary normal alcohols at T = 298.2 K
• Liquid-liquid equilibrium data for ternary systems of water + lactic acid + C4-C7 alcohols at 298.2 K and atmospheric pressure
• Thermodynamic and spectral investigations of binary liquid mixturesof 2-butoxy ethanol with alcohols at temperature range of 293.15-313.15 K
• Solubilities of crotonic acid in different organic solvents at severaltemperatures 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
• 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
• Solubility of androstenedione in lower alcohols
• Measurement and correlation of the solubility of maleic anhydride in different organic solvents
• Unusual behavior of the isotope effect on miscibility of 1-hexyl-3-methylimidazolium bis(trifluorosulfonyl)imide with 1-alkanols
• Present status of the modified UNIFAC Model for the prediction of phase equilibria and excess enthalpies for systems with ionic liquids
• Determination and correlation of solubility and solution thermodynamics of valnemulin hydrogen tartrate in different pure solvents
• Thermodynamics of risperidone and solubility in pure organic solvents
• Solid-liquid equilibrium and thermodynamic of 2,5-thiophenedicarboxylic acid in different organic solvents
• Isobaric vapor-liquid equilibrium for the binary systems of 1-butanol +Poly methoxy methylal (n=2), and 1-butanol +Poly methoxy methylal (n=3) at 101.3 kPa
• Experimental and theoretical study of interaction between organic compounds and 1- (4-sulfobutyl)-3-methylimidazolium based ionic liquids
• Liquid-liquid equilibrium of 1-butanol + water +tri-n-butyl phosphate + ammonium chloride system
• Solubility of N-Ethylcarbazole in different organic solvent at 279.15 - 319.15 K
• Solubility and tie-line data for ternary aqueous mixtures of cyclopentanol with organic solvents at T = 298.2 K: Experiments and NRTL model
• Measurement and correlation of the solubility of N-(phosphonomethyl)iminodiacetic acid in different organic solvents
• Solid-liquid equilibrium of sulbactam in pure solvents and binary solvent mixtures
• Isobaric (vapor+liquid) equilibrium for n-propyl acetate with 1-butanol or 2-butanol. Binary mixtures at 0.15 and 0.6 MPa
• Phase equilibria of the water + 1-butanol + toluene ternary system at 101.3 kPa
• Liquid-liquid equilibrium and critical states for the system acetic acid + n-butanol + n-butyl acetate + water at 308.15 K
• Isothermal vapor liquid equilibrium and molar excess Gibbs energies of two ternary systems containing either 1-butanol or 2-butanol + 1- hexene + methylbenzene at 313.15 K
• 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
• Measurement of activity coefficient at infinite dilution for some bio-oil components in water and mass transfer study of bubbles in the dilutor.
• Atmospheric densities and interfacial tensions for 1- alkanol (1-butanol to 1-octanol) + water and ether (MTBE, ETBE, DIPE, TAME and THP) + water demixed mixtures.
• Liquid-liquid equilibria for water + 1-propanol (or 1-butanol) + potassium chloride + ammonium chloride quaternary systems at 298.15 K
• Phase equilibria of (water + propionic acid or butyric acid + 2-methoxy- 2-methylpropane) ternary systems at 298.2 K and 323.2 K
• Thermodynamic analysis for determination of solid - liquid equilibrium of dibenzothiophene in a binary solvent of formic acid and butan-1-ol between (278.15 and 333.15) K
• Activity coefficients at infinite dilution for different alcohols and ketones in [EMpy][ESO4]: Experimental data and modeling with PC-SAFT
• Liquid-liquid equilibria for the ternary system containing 1-Butanol + methoxy(methoxymethoxy)methane + water at temperatures of 303.15, 323.15 and 343.15 K
• 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
• A model to calculate concentration-dependent surface tension of binary systems
• Influence of electrolytes on liquid-liquid equilibria of water/1-butanol and on the partitioning of 5-hydroxymethylfurfural in water/1-butanol
• Equilibrium study and diversified models of drug Norfloxacin in eight pure organic and binary solvents at T = (278.15 to 328.15) K
• Isothermal vapor-liquid equilibria, excess molar volume and the deviation of refractive indices for binary mixtures of 1-butanol, 1- hexanol, 3-methyl-1-butanol and butyl acetate
• Effect of composition and temperature variations on thermophysical properties of binary and ternary mixtures of 1-ethyl-3-methylimidazolium ethylsulfate with 1-butanol and /or methanol
• Evaluation of the solvent structural effect upon the vapor-liquid equilibrium of [C4C1im][Cl] + Alcohols
• 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
• High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
• The solubility of maleic acid in various inorganic salts and organic solvents: Thermodynamics model and parameters
• Thermodynamic equilibrium of hydrocortisone form I in different solvent systems
• Liquid-liquid equilibrium and critical states for the quaternary system propionic acid-n-butanol-n-butyl propionate-water at 303.15 K
• 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
• 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
• 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
• Isobaric vapor-liquid equilibrium, density and speed of sound of binary mixtures 2,2,4-trimethylpentane + 1-butanol or dibutyl ether (DBE) at 101.3 kPa
• New ionic liquid [P4,4,4,4][NTf2] in bio-butanol extraction on investigation of limiting activity coefficients
• Experimental study of the LL, VL and VLL equilibria of water + 1-butanol + 2-octanol at 101.3 kPa
• Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
• Liquid-liquid equilibrium data and thermophysical properties for ternary systems composed of water, acetic acid and different solvents
• Thermodynamic equilibrium of hexamethylenediammonium glutarate in mono-solvents and binary solvent systems
• Ammonium ionic liquids in separation of water/butan-1-ol using liquid-liquid equilibrium diagrams in ternary systems
• Dissolution behavior and thermodynamic properties of lapatinib ditosylate in pure and mixed organic solvents from T = (283.15-323.15) K
• Application of trihexyltetradecylphosphonium dicyanamide ionic liquid for various types of separations problems: Activity coefficients at infinite dilution measurements utilizing GLC method
• Quaternary liquid-liquid equilibrium, solubility and critical states: Acetic acid - n-butanol - n-butyl acetate - water at 318.15 K and atmospheric pressure
• Measurement of the thermal conductivity of biofuel mixtures: Methyl caprate components of biodiesel and alcohols
• (Vapour + liquid) equilibria of (1-butanol + benzene, or toluene, or o-, or m-, or p-xylene) at T = 308.15 K
• Isothermal and isobaric (vapour + liquid) equilibria of (alpha-pinene + n-butanol + n-octane)
• Excess molar heat capacities for (1-butanol+1,3-butanediol) at temperatures from (285 to 353) K
• Salt effect on (liquid + liquid) equilibrium of (water + tertbutanol + 1-butanol) system: Experimental data and correlation
• 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
• 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
• Phase equilibrium properties of binary and ternary systems containing di-isopropyl ether + 1-butanol + benzene at 313.15 K
• Excess molar enthalpies of dimethyl carbonate and (butanol isomers and 1-pentanol) at T = (298.15, 313.15, and 328.15) K and p = (0.1, 1.0, and 10.0) MPa
• (Liquid + liquid) equilibrium of (water + 2-propanol + 1-butanol + salt) systems at T = 313.15 K and T = 353.15 K: Experimental data and correlation
• 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
• Excess molar volumes and excess molar enthalpies of binary and ternary mixtures of 1-butanol, a tertiary amine (tri-n-butylamine or tri-n-octylamine) and n-hexane: Experimental results and ERAS-model calculations
• 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
• 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
• Compressed liquid densities of 1-butanol and 2-butanol at temperatures from 313 K to 363 K and pressures up to 25 MPa
• Excess Gibbs free energies of the binary mixtures of acetonitrile with butanols at 94.83 kPa
• 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
• Measurement of activity coefficients at infinite dilution in 1-hexadecyl-3-methylimidazolium tetrafluoroborate ionic liquid
• Excess enthalpy, density, and speed of sound determination for the ternary mixture (methyl tert-butyl ether + 1-butanol + n-hexane)
• Molar heat capacities for (1-butanol + 1,4-butanediol, 2,3-butanediol, 1,2-butanediol, and 2-methyl-2,4-pentanediol) as function of temperature
• Study of densities, viscosities, and speeds of sound of binary liquid mixtures of butan-1-ol with n-alkanes (C6, C8, and C10) at T = (298.15, 303.15, and 308.15) K
• Density, viscosity, refractive index, excess molar enthalpy, viscosity, and refractive index deviations for the (1-butanol + 2-butanone) binary system at T = 303 K. A new adiabatic calorimeter for heat of mixing
• 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
• Measurements of activity coefficients at infinite dilution of aromatic and aliphatic hydrocarbons, alcohols, and water in the new ionic liquid [EMIM][SCN] using GLC
• Mixing thermodynamic properties of 1-butyl-4-methylpyridinium tetrafluoroborate [b4mpy][BF4] with water and with an alkan-1ol (methanol to pentanol)
• Liquid phase equilibria of (water + phosphoric acid + 1-butanol or butyl acetate) ternary systems at T = 308.2 K
• Activity coefficients at infinite dilution of hydrocarbons, alkylbenzenes, and alcohols in the paramagnetic ionic liquid 1-butyl-3-methyl-imidazolium tetrachloridoferrate(III) using gas liquid chromatography
• Activity coefficients at infinite dilution 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
• Phase equilibria study of the binary systems (N-butyl-4-methylpyridinium tosylate ionic liquid + an alcohol)
• (Vapour + liquid) equilibrium and excess Gibbs functions of ternary mixtures containing 1-butanol or 2-butanol, n-hexane, and 1-chlorobutane at T = 298.15 K
• 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
• Molar excess enthalpies at T = 298.15 K for (1-alkanol + dibutylether) systems
• Excess enthalpies of binary and ternary mixtures containing dibutyl ether (DBE), 1-butanol, and heptane at T = 298.15 K and 313.15 K
• Thermophysical properties of the binary mixtures (1,8-cineole + 1-alkanol) at T = (298.15 and 313.15) K and at atmospheric pressure
• Thermodynamic and transport properties of (1-Butanol + 1,4-Butanediol) at temperatures from (298.15 to 318.15) K
• 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
• Volumetric properties, viscosity and refractive index of the protic ionic liquid, pyrrolidinium octanoate, in molecular solvents
• Isobaric (vapour + liquid) equilibria for the (1-propanol + 1-butanol) binary mixture at (53.3 and 91.3) kPa
• A thermodynamic study on solubility and liquid-liquid phase behaviour for 2,2,2-trifluoroethanol + cyclohexane + 1-butanol at three temperatures and pressure 101.3 kPa
• 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.
• (Liquid + liquid) equilibrium of {water + phenol + (1-butanol, or 2-butanol, or tert-butanol)} systems
• 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
• Application of the ERAS model to volumetric properties of binary mixtures of banana oil with primary and secondary alcohols (C1- C4) at different temperatures
• Thermophysical properties and phase equilibria study of the binary systems {N-hexylquinolinium bis(trifluoromethylsulfonyl)imide + aromatic hydrocarbons, or an alcohol}
• 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
• (Liquid + liquid) equilibria in {water + acrylic acid + (1-butanol, or 2-butanol, or 1-pentanol)} systems at T = 293.2 K, T = 303.2 K, and T = 313.2 K and atmospheric pressure
• 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
• Volumetric properties and enthalpies of solution of alcohols CkH2k+1OH (k = 1, 2, 6) in 1-methyl-3-alkylimidazolium bis(trifluoromethylsulfonyl)imide {[C1CnIm][NTf2] n = 2, 4, 6, 8, 10} ionic liquids
• Liquid density of biofuel mixtures: (Dibutyl ether + 1-butanol) system at pressures up to 140 MPa and temperatures from (293.15 to 393.15) K
• 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
• Thermodynamic characterization of the mixture (1-butanol + iso-octane): Densities, viscosities, and isobaric heat capacities at high pressures
• Volumetric and surface properties of pure ionic liquid n-octyl-pyridinium nitrate and its binary mixture with alcohol
• PrhoT measurements and derived properties of liquid 1-alkanols
• Combined effects of salinity and temperature on the solubility of 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
• Effect of temperature and composition on the density, viscosity, surface tension, and thermodynamic properties of binary mixtures of N-octylisoquinolinium bis{(trifluoromethyl)sulfonyl}imide with alcohols
• Volumetric properties of ternary (IL + 2-propanol or 1-butanol or 2-butanol + ethyl acetate) systems and binary (IL + 2-propanol or 1-butanol or 2-butanol) and (1-butanol or 2-butanol + ethyl acetate) systems
• 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
• Experimental study on the calorimetric data of cyclohexanol with alkanols (C1-C4) and correlation with Wilson, NRTL and UNIQUAC models at 300 K
• 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
• Extraction of butan-1-ol from water with ionic liquids at T = 308.15 K
• 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
• 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
• 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
• Physicochemical properties and activity coefficients at infinite dilution for organic solutes and water in a novel bicyclic guanidinium superbase-derived protic ionic liquid
• Properties of pure n-butylammonium nitrate ionic liquid and its binary mixtures of with alcohols at T = (293.15 to 313.15) K
• Isothermal (vapour + liquid) equilibria for binary mixtures of diisopropyl ether with (methanol, or ethanol, or 1-butanol): Experimental data, correlations, and predictions
• Solubilities of evodiamine in twelve organic solvents from T = (283.2 to 323.2) K
• Ultrasonic study of molecular interactions in binary mixtures of methyl acrylate with 1-alkanols (C4 to C10) at temperatures from (288.15 to 318.15) K
• Thermodynamics of 1-alkanol + linear polyether mixtures
• Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds Part II: C18 fatty acids
• Experimental and theoretical study on infinite dilution activity coefficients of various solutes in piperidinium ionic liquids
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpyrrolidinium trifluorotris(perfluoroethyl)phosphate
• On the solubility of nicotinic acid and isonicotinic acid in water and organic solvents
• Osmotic and apparent molar properties of binary mixtures alcohol + 1-butyl-3-methylimidazolium trifluoromethanesulfonate ionic liquid
• Measurements of activity coefficients at infinite dilution for organic solutes and water in N-hexylisoquinolinium thiocyanate, [HiQuin][SCN] using GLC
• Solubility and phase behavior of binary systems containing salts based on transitional metals
• Vapour-liquid equilibria of binary and ternary mixtures containing 1-butanol, 2,2,4-trimethylpentane and 1-hexene at T = 313.15 K
• Study of surface tension and surface properties of binary systems of DMSO with long chain alcohols at various temperatures
• Density and surface tension of pure ionic liquid 1-butyl-3-methylimidazolium L-lactate and its binary mixture with alcohol and water
• 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
• Volumetric behaviour of the (2,2,4-trimethylpentane + methylbenzene + butan-1-ol) ternary system and its binary sub-systems within the temperature range (298.15-328.15) K
• Vapour pressures and osmotic coefficients of binary mixtures containing alcohol and pyrrolidinium-based ionic liquids
• 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
• Solubility of carbon dioxide, methane, and ethane in 1-butanol and saturated liquid densities and viscosities
• 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
• Thermodynamics and activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylmorpholinium tricyanomethanide
• Thermodynamic and acoustic properties of binary mixtures of 1-butanol with 1,2-butanediol. The comparison with the results for 1,3-, and 1,4-butanediol
• 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
• 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-hexyl-1,4-diaza[2.2.2]bicyclooctanium bis(trifluoromethylsulfonyl)imide using gas-liquid chromatography
• Tie line data for the (water + butyric acid + n-butyl alcohol or amyl alcohol) at T = (298.2, 308.2, and 318.2) K and (water + butyric acid + isoamyl alcohol) at T = 298.2 K
• Osmotic coefficients of alcoholic mixtures containing BMpyrDCA: Experimental determination and correlation
• Determination and correlation of the solubility of four Bronsted-acidic ionic liquids based on benzothiazolium cations in six alcohols
• Densities, viscosities, and isobaric heat capacities of the system (1-butanol + cyclohexane) at high pressures
• 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
• (Solid + liquid) phase equilibria of tetraphenyl piperazine-1,4-diyldiphosphonate in pure solvents
• 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
• Isothermal (liquid + liquid) equilibrium data at T = 313.15 K and isobaric (vapor + liquid + liquid) equilibrium data at 101.3 kPa for the ternary system (water + 1-butanol + p-xylene)
• VLE measurements using a static cell vapor phase manual sampling method accompanied with an empirical data consistency test
• A combined experimental and computational investigation of excess molar enthalpies of (nitrobenzene + alkanol) mixtures
• Thermodynamics of 4'-bromomethyl-2-cyanobiphenyl in different solvents
• Experimental and theoretically study of interaction between organic compounds and tricyanomethanide based ionic liquids
• Solubility and solution thermodynamics of sorbic acid in eight pure organic solvents
• 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
• Isothermal (vapour + liquid) equilibrium and thermophysical properties for (1-butyl-3-methylimidazolium iodide + 1-butanol) binary system
• Solubility of daidzin in different organic solvents and (ethyl alcohol + water) mixed solvents
• 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
• Activity coefficients at infinite dilution for organic solutes and water in 1-ethyl-1-methylpyrrolidinium lactate
• Measurement and correlation of the solubility of genistin in eleven organic solvents from T = (283.2 to 323.2) K
• Activity coefficients at infinite dilution, physicochemical and thermodynamic properties for organic solutes and water in the ionic liquid ethyl-dimethyl-(2-methoxyethyl)ammonium trifluorotris-(perfluoroethyl)phosphate
• Measurement and correlation of the solubility of 3,4-bis(3-nitrofurazan-4-yl)furoxan (DNTF) in different solvents
• Measurements and equation-of-state modelling of thermodynamic properties of binary mixtures of 1-butyl-1-methylpyrrolidinium tetracyanoborate ionic liquid with molecular compounds
• Volumetric behavior of the ternary system (methyl tert-butyl ether + methylbenzene + butan-1-ol) and its binary sub-system (methyl tert-butyl ether + butan-1-ol) within the temperature range (298.15 to 328.15) K
• (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
• Solubility measurement and modelling of 1,8-dinitronaphthalene in nine organic solvents from T = (273.15 to 308.15) K and mixing properties of solutions
• Screening of environmental friendly ionic liquid as a solvent for the different types of separations problem: Insight from activity coefficients at infinite dilution measurement using (gas + liquid) chromatography technique
• 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
• Feasibility of bio-based lactate esters as extractant for biobutanol recovery: (Liquid + liquid) equilibria
• Speed of sound measurements of liquid C1-C4 alkanols
• Solubility modelling and thermodynamic dissolution functions of phthalimide in ten organic solvents
• Ternary (liquid + liquid) equilibria of {bis(trifluoromethylsulfonyl)-amide based ionic liquids + butan-1-ol + water}
• Thermodynamic models for determination of the solubility of omeprazole in pure and mixture organic solvents from T = (278.15 to 333.15) K
• Solubility of rosuvastatin calcium in different neat solvents at different temperatures
• Solubility and solution thermodynamics of ethyl 5-amino-4-cyano-3-(2-ethoxy-2-oxoethyl)-2-thiophenecarboxylate in nine organic solvents at evaluated temperatures
• Ionic association and conductance of [emim][BF4] and [bmim][BF4] in 1-butanol in a wide range of temperature
• 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
• Solubility measurement and thermodynamic functions of dehydroepiandrosterone acetate in different solvents at evaluated temperatures
• (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
• Isobaric vapor-liquid-liquid-solid equilibrium of the water + NaCl + 1-butanol system at 101.3 kPa
• 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 thermodynamic function of a bioactive compound bergenin in various pharmaceutically acceptable neat solvents at different temperatures
• Determination and correlation of solubility and thermodynamic properties of pyraclostrobin in pure and binary solvents
• (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
• Thermodynamic study of the solubility of 2,4'-dihydroxydiphenyl sulfone in nine organic solvents from T = (278.15 to 313.15) K and thermodynamic properties of dissolution
• Thermodynamic and spectroscopic interpretation of molecular interactions of nicotine + alcohol binary mixtures
• Viscosities of binary mixtures containing 1-butanol + 2,2,4-trimethylpentane or + 1,2,4-trimethylbenzene at high pressures for the thermophysical characterization of biofuels
• 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
• Determination and correlation thermodynamic models for solid liquid equilibrium of the Nifedipine in pure and mixture organic solvents
• Measurement and modelling of econazole nitrate in twelve pure organic solvents at temperatures from 278.15 K to 318.15 K
• 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
• Solubility measurement and correlation of the form A of ibrutinib in organic solvents from 278.15 to 323.15 K
• Solubility measurement and modelling of ethyl 5-amino-4-cyano-3-(2-ethoxy-2-oxoethyl)-2-thiophenecarboxylate in four groups mixed solvents
• 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
• Investigation on molecular interactions of antibiotics in alcohols using volumetric and acoustic studies at different temperatures
• Solubility determination and thermodynamic modeling of paclobutrazol in nine organic solvents from T = (278.15 to 318.15) K and mixing properties of solutions
• Measurement and correlation of solubility of ciclesonide in seven pure organic 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
• 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
• 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 properties of vanillyl alcohol in some pure solvents
• Thermodynamic models for determination of solid liquid equilibrium of the 6-benzyladenine in pure and binary organic solvents
• 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
• Thermodynamic equilibrium of hydroxyacetic acid in pure and binary solvent systems
• 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
• 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
• Thermophysical properties of 1,2,4-trimethylbenzene in admixtures with 1-butanol or 2-butanol at high pressures
• Thermodynamic properties of enantiotropic polymorphs of glycolide
• Liquid-liquid equilibrium in systems used for the production of 5-hydroxymethylfurfural from biomass using alcohols as solvents
• Thermodynamic study of solubility for pyrazinamide in ten solvents from T = (283.15 to 323.15) K
• 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
• Mutual diffusion coefficients of n-butanol + n-heptane and n-pentanol + n-heptane from 288.15 K to 318.15 K
• Physical properties of systems of interest to the edible oil industry: Viscosities and densities of model systems formed by (triacylglycerol + fatty acid + solvent)
• Thermodynamics and activity coefficients at infinite dilution for organic compounds and water in the ionic liquid 1-butyl-3-methylimidazolium perchlorate
• Measurement and correlation of isobaric vapour-liquid equilibria for binary systems of 1-(methoxymethoxy)-2-methyl-propane with 1-butanol and isobutanol at 101.33 kPa
• 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
• 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
• Excess molar enthalpies of R-fenchone + butan-1-ol or + pentan-1-ol. Modeling with COSMO-RS and UNIFAC
• Thermodynamic study of molecular interaction-selectivity in separation processes based on limiting activity coefficients
• Phase equilibria of the water + 1-butanol + 2-pentanol ternary system at 101.3 kPa
• Isobaric heat capacity of nanostructured liquids with potential use as lubricants
• Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in ionic liquid [HMMIM][BF4]
• 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
• 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
• Determination of the thermodynamic parameters of ionic liquid 1-propyl-3-methylimidazolium bromide by gas-liquid chromatography
• 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
• Thermodynamic properties of paracetamol impurities 4-nitrophenol and 4'-chloroacetanilide and the impact of such impurities on the crystallisation of paracetamol from solution
• Separation of water/butan-1-ol with ionic liquids in ternary liquid-liquid phase equilibrium
• Volumetric and sound speed study of aqueous 1-butanol liquid mixtures at different temperatures
• Surface tension and interfacial compositions of binary glycerol/alcohol mixtures
• Determination and correlation of solubility and solution thermodynamics of musk xylene in different pure solvents
• Separation of (water/butan-1-ol) binary systems based on activity coefficients at infinite dilution with phosphonium ionic liquid
• Solubility behaviour and thermodynamic analysis of methyleneaminoacetonitrile in binary (ethanol + water, ethanol + 2-propanol, ethanol + n-butanol) solvents
• 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
• Enthalpies of dilution of aqueous solutions of n-butanol, butanediols, 1,2,4-butanetriol, and 1,2,3,4-butanetetrol at 298.15K
• 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
• Thermophysical properties and thermodynamic phase behavior of ionic liquids
• Excess molar enthalpies and heat capacities of dimethyl sulfoxide + seven normal alkanols at 303.15K and atmospheric pressure
• Excess molar enthalpies for binary mixtures of trimethyl phosphate with alkanols {CH3(CH2)nOH, n = 0 3} at 298.15K
• Studies of viscosities of dilute solutions of alkylamines in non-electrolyte solvents III. Alkylamines in butanols 303.15K
• Volumetric and transport properties of ternary mixtures containing 1-alkanol + ethyl ethanoate + cyclohexane at 303.15 K: Experimental data, correlation and prediction by ERAS model
• Topological investigations of the molecular species and molecular interactions that characterize pyrrolidin-2-one + lower alkanol mixtures
• Experimental determination and modelling of densities and excess molar volumes of ternary system (1-butanol + cyclohexylamine + n-heptane) and corresponding binaries from 288.15 to 323.15K
• Excess molar volumes of Diisopropylamine + (C1-C5) Alkan-1-ols: application of the ERAS model and cubic EOS
• Thermodynamic properties of binary liquid mixtures of diethylenetriamine with alcohols at different temperatures
• Experimental Determination and Modeling of Densities and Refractive Indices of the Binary Systems Alcohol + Dicyclohexylamine at T = (288.15 to 323.15) K
• Experimental Determination and Modeling of Densities, Refractive Indices of the Binary Mixtures of Dimethylphthalate (or Dimethyladipate) + 1-Butanol, or + 2-Butanol, or + 2-Butanone at T = (288.15 to 323.15) K
• Solubilities of succinimide in different pure solvents and binary methanol+ethyl acetate solvent mixtures
• Measurement and Correlation for Solubility of Dexibuprofen in Different Solvents from (263.15 to 293.15) K
• Determination of the solubility, dissolution enthalpy and entropy of 3-pentadecylphenyl acrylate in different organic solvents
• Thermodynamic behavior of binary mixtures CnMpyNTf2 ionic liquids with primary and secondary alcohols
• Thermogravimetric measurement of evaporation: Data analysis based on the Stefan tube
• Thermodynamics of mixtures containing amines. XVI. CE pm of 1-butanol, 1-octanol or 1-decanol + benzylamine systems at (298.15, 308.15, 318.15 and 333.15) K
• Effects of alkyl group and temperature on the interactions between furfural and alcohol: Insight from density and sound velocity studies
• 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
• Determination and correlation of solubility and mixing properties of isonicotinamide (form II) in some pure solvents
• Experimental and theoretical excess molar properties of imidazolium based ionic liquids with isomers of butanol
• Renewable platform chemicals: Thermochemical study of levulinic acid esters
• Measurement and correlation of solubility of carbendazim in lower alcohols
• Solubility and Caloric Properties of Cinnarizine
• Experimental and Computational Thermodynamic Properties of (Benzyl alcohol + Alkanols) Mixtures
• Thermodynamic Behaviour of Binary Mixtures of 1-Butyl-1- methylpyrrolidinium Iodide and Alcohols
• Solubility and Solution Thermodynamics of Gibberellin A4 in Different Organic Solvents from 278.15 K to 333.15 K
• Solid Forms, Crystal Habits, and Solubility of Danthron
• Density, Speed of Sound, Viscosity, Excess Properties, and Prigogine Flory Patterson (PFP) Theory of Binary Mixtures of Amine and Alcohols
• Solubility of Amorphous Clopidogrel Hydrogen Sulfate in Different Pure Solvents
• Density, Refractive Index, and Sound Velocity for the Binary Mixtures of Tri-n-Butyl Phosphate and n-Butanol between 303.15 K and 323.15 K
• Vapor-Liquid Equilibrium of Binary Mixtures Containing Isopropyl Acetate and Alkanols at 101.32 kPa
• Density and Excess Molar Volumes of 1-Butanol + Methanol + Electrolyte Systems in the Temperature Range (293.15 308.15) K
• Solubility Measurement and Correlation for 2- Naphthaldehyde in Pure Organic Solvents and Methanol + Ethanol Mixtures
• Solubility and Thermodynamic Analysis of Tenoxicam in Different Pure Solvents at Different Temperatures
• Tie-Line Data for Aqueous Mixtures of Butyric Acid with Diisopropyl Ether at Various Temperatures
• Thermodynamic Analysis of the Experimental Equilibria for the Liquid-Phase Etherification of Isobutene with C1 to C4 Linear Primary Alcohols
• Solubility of Agomelatine Crystal Form I and Form II in Pure Solvents and (Isopropanol + Water) Mixtures
• 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 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
• Solubility Determination and Modeling of Sodium Mononitrobenzenesulphonate in Different Solvents at Temperatures Ranging from (283.15 to 323.15) K
• Solid Liquid Phase Equilibrium of trans-Cinnamic Acid in Several Alcohols: Measurements and Thermodynamic Modeling
• Thermodynamics of 1,3-dimethylurea in eight alcohols
• Measurements of Infinite Dilution Activity Coefficients of Alkanols in the Ionic Liquid Tributylmethylammonium Methyl Sulfate Using HS-SPME/GC/FID
• 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
• Isobaric Vapor Liquid Equilibrium for Two Binary Systems (n-Butanol + 1,4-Butanediol and .gamma.-Butyrolactone + 1,4-Butanediol) at p = (30.0, 50.0, and 70.0) kPa
• 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
• Determination and Correlation of Solubility of 3,4-Dinitro-1H-pyrazole in Different Pure Solvents from 298.15 K to 338.15 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
• Isobaric Vapor Liquid Equilibrium for the Binary Systems of sec-Butyl Acetate + n-Butyl Alcohol, Isobutyl Alcohol, or tert-Butyl Alcohol at 101.3 kPa
• Isobaric Vapor Liquid Equilibrium for Two Binary Systems (Methanol + Dibutyl Carbonate) and (n-Butanol + Dibutyl Carbonate) at p = 40.0, 70.0, and 100.0 kPa
• 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
• Solubility Measurement and Correlation of Two Erlotinib Hydrochloride Polymorphs in Alcohols and Ketones from 273.15 to 323.15 K
• Ternary Liquid Liquid Equilibrium of Azeotropes (Ester + Alcohol) with Different Ionic Liquids at T = 298.15 K
• Determination and Correlation of Solubility of Phenylbutazone in Monosolvents and Binary Solvent Mixtures
• Solubilities of 4',5,7-Triacetoxyflavanone in Fourteen Organic Solvents at Different Temperatures
• Liquid Liquid Equilibrium Data of Water + Butyric Acid + {Butanal or n-Butanol} Ternary Systems at 293.15, 308.15, and 323.15 K
• Measurement and Correlation of the Solubility of 2,6-Dihydroxybenzoic Acid in Alcohols and Binary Solvents
• Phase Behavior of Binary Mixtures Containing Succinic Acid or Its Esters
• Isobaric Vapor Liquid Equilibrium for the Binary Systems Dimethyl Disulfide + C1 C4 n-Alkanol at 40.000 and 101.325 kPa
• Pressurized-Synthetic Methodology for Solubility Determination at Elevated Temperatures with Application to Paracetamol in Pure Solvents
• Compressed Liquid Densities of Binary Mixtures of 1-Butanol and Diethylene Glycol Dimethyl Ether from (283 to 363) K at Pressures up to 100 MPa
• Isobaric Vapor Liquid Equilibrium for Three Binary Systems of Acetaldehyde + Ethanol, Ethyl Acetate, 1-Butanol at 101.3 kPa
• Solubility of Benzoin in Six Monosolvents and in Some Binary Solvent Mixtures at Various Temperatures
• Measurement and Correlation of Solubility of Two Isomers of Cyanopyridine in Eight Pure Solvents from 268.15 K to 318.15 K
• Measurement and Correlation of Liquid Liquid Equilibria for the Ternary Systems of Water + d-Fructose + 1-Butanol, Water + d-Glucose + 1-Butanol, and Water + d-Galactose + 1-Butanol at (288.2, 303.2 and 318.2) K
• Solubility and Thermodynamic Behavior of Syringic Acid in Eight Pure and Water + Methanol Mixed Solvents
• Measurement and Correlation of Isobaric Vapor Liquid Equilibrium for Binary Systems of 1-(Ethoxymethoxy)-2-methyl-propane with Isobutyl Alcohol or 1-Butanol at 101.33 kPa
• Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Butanol, + Isobutyl Alcohol, or + 2-Butanol from 293.15 to 333.15 K at 0.1 MPa
• Determination and Correlation of Solubility of Quetiapine Fumarate in Nine Pure Solvents and Two Aqueous Binary Solvents
• Solubility Modeling and Mixing Thermodynamics of Thiamphenicol in Water and Twelve Neat Organic Solvents from T = (278.15 to 318.15) K
• Extraction of Citric Acid and Maleic Acid from Their Aqueous Solutions Using a Phosphorus-Bonded Extractant, Tri-n-octylphosphineoxide, and a Secondary Amine, Dioctylamine
• Liquid-Liquid Equilibrium for Ternary System n-Butanol + n-Hexane + Ethylene Glycol at 298.15-323.15 K
• Thermodynamic Functions for the Solubility of 3-Nitrobenzonitrile in 12 Organic Solvents from T/K = (278.15 to 318.15)
• Densities and Viscosities for Binary Liquid Mixtures of Butan-1-ol + Propane-1,2-diol, + Butane-1,2-diol and 2-Methylpropan-1-ol + Propane-1,2-diol, + Butane-1,2-diol from 298.15 to 333.15 K at 0.1 MPa
• Liquid-Liquid Extraction of Butanol from Heptane + Butanol Mixture by Ionic Liquids
• 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
• Liquid-Liquid Equilibria Determination and Prediction for Ternary Systems of Water + 1,6-Hexanediamine + (1-Butanol or 1-Pentanol) at 298.2, 308.2, and 318.2 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
• Experimental Vapor-Liquid Equilibria and Thermodynamic Modeling of the Methanol + n-Heptane and 1-Butanol + Aniline Binary Systems
• 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
• Determination and Thermodynamic Analysis of the Solubility of Limonin in Eight Organic Solvents and Ethyl Acetate + 2-Propanol Binary Solvents from 283.2 to 323.2 K
• Solubility of 2,5-Furandicarboxylic Acid in Eight Pure Solvents and Two Binary Solvent Systems at 313.15-363.15 K
• Dibutyl Citrate Synthesis, Physicochemical Characterization, and Px Data in Mixtures with Butanol
• Experimental Binary VLE Data of Morpholine with 1-Butanol and 3-Methyl-1-butanol Systems
• Solubility of Sulfachloropyridazine in Pure and Binary Solvent Mixtures and Investigation of Intermolecular Interactions
• Measurement and Correlation of the Solubility of Florfenicol Form A in Several Pure and Binary Solvents
• Liquid-Liquid Equilibrium for Ternary Systems, Water + 5-Hydroxymethylfurfural + (1-Butanol, Isobutanol, Methyl Isobutyl Ketone), at 313.15, 323.15, and 333.15 K
• Measurement and Correlation of the Solubility of Pyrimethanil in Seven Monosolvents and Two Different Binary Mixed Solvents
• Solubility of Acetylene in Alcohols and Ketones
• 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
• Measurement and Modelization of VLE for Butyl Acetate with Methanol, Ethanol, 1-Propanol, and 1-Butanol. Experimental Data at 0.15 MPa
• 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)
• Research on Dissolution Capability of Several Antofloxacin Salts
• Study of the LLE, VLE, and VLLE of the Ternary System Water + 1-Butanol + Isoamyl Alcohol at 101.3 kPa
• 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
• Densities and Viscosities of Ternary System n-Dodecane (1) + Bicyclohexyl (2) + n-Butanol (3) and Corresponding Binaries at T = (293.15 to 333.15) K
• Isobaric Vapor-Liquid Equilibrium for the Binary Systems of 2-Butanol + 2-(Methoxymethoxy)-butane and 1-Butanol + 2-(Methoxymethoxy)-butane at 101.3 kPa
• Thermodynamic Study of Solubility for Imatinib Mesylate in Nine Monosolvents and Two Binary Solvent Mixtures from 278.15 to 318.15 K
• Solubility Determination of Nicotinamide and Its Application for the Cocrystallization with Benzoic Acid
• 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)
• Measurement of Critical Properties for Binary and Ternary Mixtures Containing n-Butanol and n-Alkane
• 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
• Viscosity and Density of n-Alcohols at Temperatures between (298.15 and 323.15) K and Pressures up to 30 MPa
• 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
• 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
• Solubility of N-tert-Butylbenzothiazole-2-sulfenamide in Several Pure and Binary Solvents
• 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 Behavior of 2-Chloro-3- (trifluoromethyl)pyridine in (Ethyl Acetate + n-Butanol, DMF + n-Butanol, DMF + Ethanol) Solvent Mixtures
• Liquid-Liquid Equilibria Data of Protic Ionic Liquid (Ethyl-2-hydroxyethylammonium Propionate, Diethylammonium Propionate, or Butylammonium Propionate) with 1-Butanol + Water at 298.15 K
• Solubility Modeling and Solvent Effect of 2-Amino-6-chloropurine in Twelve Neat Solvents
• 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
• 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
• Comparison of Extractability of Oxalic Acid from Dilute Aqueous Solutions Using Dioctylamine and Trioctylphosphine Oxide
• Binary Solid-Liquid Solubility Determination and Model Correlation of Quizalofop-p-ethyl in Different Pure 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
• Liquid-Liquid Equilibrium Measurements and Correlation for Ternary Systems (Butyl Acetate + 1-Butanol + Ethylene Glycol/1,3-Propanediol/Ethanolamine) at 298.15 K
• 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
• Equilibrium Solubility, Model Correlation, and Solvent Effect of Indole-3-acetic Acid in Twelve Pure Solvents
• Solubility Determination and Modeling of p-Nitrobenzamide Dissolved in Twelve Neat Solvents from 283.15 to 328.15 K
• Isothermal Vapor-Liquid Equilibrium Measurements for the Pentan-2-one + Propan-1-ol/Butan-1-ol System within 342-363 K
• Thermodynamic Models for Determination of Solid-Liquid Equilibrium of the Buprofezin in Pure and Binary Organic Solvents
• 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
• Separation of Butanol Using Tetradecyl(trihexyl)phosphonium Bis(2,4,4-trimethylpentyl)phosphinate, Oleyl Alcohol, and Castor Oil
• Solubility Determination and Model Correlation of Pymetrozine and Evaluation of the Effect of Solvent Properties and Composition
• 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 and Solvent Effect of Acetamiprid in Thirteen Pure Solvents and Aqueous Solutions of Ethanol
• Design of a Salt-Free Aqueous Two-Phase System Containing Butanol, n-Butylpyridine Dicyanamide, and Water: Equilibrium Data and Correlation
• Solubility Measurement and Correlation of 2-Oxindole in 12 Pure Organic Solvents
• Determination and Correlation of the Solubility of Musk Ketone in Pure and Binary Solvents at 273.15-313.15 K
• 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
• 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, Solubility Modeling, and Antisolvent Precipitation of 1,3-Bis(9-carbazolyl)benzene in Organic Solvents
• 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
• The Research and Measurement about the Solubility of l-Serine in Eight Common Pure Solvents and Four Binary Mixed Solvents for T = (278.15-333.15) K
• Isobaric Vapor Liquid Equilibrium Data for the 1,2-Dichloroethane-1-Butanol System
• 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
• Vapor-Liquid Equilibrium for Binary of 1-Butanol + N,N-Dimethylacetamide and Methyl Isobutyl Ketone + N,N-Dimethylacetamide at 101.3 kPa
• Solubility and Solvent Effect of 1-(2-Bromo-phenyl)-pyrrole-2,5-dione in 14 Pure Solvents from 278.15 to 323.15 K
• Saturated Solubility and Thermodynamic Evaluation of l-Tryptophan in Eight Pure Solvents and Three Groups of Binary Mixed Solvents by the Gravimetric Method at T = 278.15-333.15 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 measurement and thermodynamic model correlation of sancycline in twelve pure solvents
• 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
• Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
• Isobaric Phase Equilibria of Diethyl Carbonate with Five Alcohols at 101.3 kPa
• 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
• Mixing Properties for the Ternary Mixture Methyl tert-Butyl Ether + 1-Butanol + Decane at 298.15 K
• Bubble Temperatures of the Binary Mixtures of Dimethylcarbonate with Some Alcohols at 95.8 kPa
• Viscosities and Densities of Binary Mixtures of 1,4-Dioxane, Carbon Tetrachloride, and Butanol at 303.15 K, 308.15 K, and 313.15 K
• Bubble-Temperature Measurements on Some Binary Mixtures Formed by Tetrahydrofuran or Amyl Alcohol with Hydrocarbons, Chlorohydrocarbons, or Butanols at (94.6 or 95.8) kPa
• Viscosities of Binary Mixtures of Isomeric Butanols or Isomeric Chlorobutanes with 2-Methyltetrahydrofuran
• 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
• Liquid-Liquid Equilibria of Water + 1-Butanol + 2-Ethyl-1-hexanol System
• Measurement and Correlation of Excess Molar Enthalpies for Ethylene Glycol + Alkanol Systems at the Temperatures (298.15, 308.15, and 323.15) K
• Vapor-Liquid Equilibrium Studies for Systems Containing n-Butylisocyanate at Temperatures between 323.15 K and 371.15 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
• Liquid-Liquid Equilibria of Room Temperature Ionic Liquids and Butan-1-ol
• Density, Surface Tension, and Refractive Index of Octane + 1-Alkanol Mixtures at T ) 298.15 K.
• 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
• Henry's Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, Isobutane, 1-Butene, Isobutene, trans-2-Butene and 1,3-Butadiene in 1-Butanol and 2-Butanol at (250 to 330) K
• 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
• Density, Viscosity, Refractive Index, and Speed of Sound for Binary Mixtures of 1,4-Dioxane with Different Organic Liquids at (298.15, 303.15, and 308.15) K
• Densities and Viscosities of Binary Mixtures of 1-Chlorobutane with Butanol Isomers at Several Temperatures
• Measurement of Diffusion Coefficients in Thermodynamically Nonideal Systems
• Thermodynamic Properties of dodecane + 1-butanol and + 2-butanol systems
• Excess Molar Volumes and Surface Tensions of 1,2,4-Trimethylbenzene and 1,3,5-Trimethylbenzene with 1-Butanol, 2-Methyl-1-propanol, 2-Butanol, and 2-Methyl-2-propanol at 298.15 K
• Thermodynamics of Phase and Chemical Equilibrium in a Strongly Nonideal Esterification System.
• Thermochemistry of Benzyl Alcohol: Reaction Equilibria Involving Benzyl Alcohol and tert-Alkyl Ethers
• Excess Enthalpy, Density, Viscosity, and Speed of Sound for the Mixture Tetrahydropyran + 1-Butanol at (283.15, 298.15 and, 313.15) K
• Solubilities of Proxetine Hydrochloride Hemihydrate between 286 K and 363 K
• Isothermal Vapor-Liquid Equilibria for the n-Pentane + 1-Butanol and n-Pentane + 2-Butanol Systems near the Critical Region of the Mixtures
• Viscosities, Densities, and Ultrasonic Velocities of Binary Mixtures of Ethylbenzene with Ethanol, 1-Propanol, and 1-Butanol at (298.15 and 308.15)K
• High-Pressure Vapor-Liquid Equilibria in the System Carbon Dioxide + 1-Butanol at Temperatures from (293.15 to 324.15) K
• Concentration Dependence of Surface Tension for Very Dilute Aqueous Solutions of Organic Non-Electrolytes
• Solubility and Density of 2,6-Dimethylnaphthalene in C1-C7 1-Alkanols
• Surface Tension of Dilute Solutions of Linear Alcohols in Benzyl Alcohol
• Densities and Viscosities of Binary Mixtures of 1-Bromobutane with Butanol Isomers at Several Temperatures
• 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 and Viscosity for Ethyl 3-Ethoxypropionate + Methacrylic Acid, + Benzyl Methacrylate, and + 2-Hydroxyethyl Methacrylate
• Solubility of Cefazolin Sodium Pentahydrate in Different Solvents between 275 K and 310 K
• Excess Enthalpy, Density, and Speed of Sound for the Mixtures a-Pinene + 1-Butanol or 2-Butanol at (283.15, 298.15, and 313.15) 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
• Solubility of Organic Systems Containing 1,4-Dioxan-2-one
• Solubility of Berberine Chloride in Various Solvents
• 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
• Liquid-Liquid Equilibria of the System 1-(2-Hydroxyethyl)-3-methylimidozolium Tetrafluoroborate or 1-(2-Hydroxyethyl)-2,3-dimethylimidozolium Tetrafluoroborate + Water + 1-Butanol at 293.15 K
• Liquid-Liquid Equilibrium in Mixtures of the Ionic Liquid 1-n-Butyl-3-methylimidazolium Hexafluorophosphate and an Alkanol
• Density and Surface Tension of Binary Mixtures of Acetonitrile + 1-Alkanol at 293.15 K
• Vapor-Liquid Equilibrium of Binary Mixtures. 1. Ethanol + 1-Butanol, Ethanol + Octane, 1-Butanol + Octane
• Vapor-Liquid Equilibrium of Binary Mixtures. 2. Ethanol + 2,2,4-Trimethylpentane, 1-Butanol + 2,2,4-Trimethylpentane, and Ethanol + o-Xylene
• Excess Enthalpy, Density, Speed of Sound, and Viscosity for 2-Methyltetrahydrofuran + 1-Butanol at (283.15, 298.15, and, 313.15) K
• 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
• Densities and Viscosities of Binary Mixtures of 1-Butanol with Methacrylic Acid, Benzyl Methacrylate, and 2-Hydroxyethyl Methacrylate between 288.15 K and 318.15 K
• Measurement and Correlation of Solubilities of Luteolin in Organic Solvents at Different Temperatures
• Density and Surface Tension Variation with Temperature for Heptane + 1-Alkanol
• 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
• Effect of Pressure on the Static Relative Permittivities of Alkan-1-ols at 298.15 K
• Liquid-Liquid Equilibrium in Binary System [bmim][PF6] + 1-Butanol
• 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
• Solubility of Xylitol in Ethanol, Acetone, N,N-Dimethylformamide, 1-Butanol, 1-Pentanol, Toluene, 2-Propanol, and Water
• 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
• Viscosities and Interfacial Properties of I-Methyl-3-butylimidazolium Hexafluorophosphate and 1-Isobutenyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
• Solubility of Clopidogrel Hydrogen Sulfate (Form II) in Different Solvents
• 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 Artemisinin in Different Single and Binary Solvent Mixtures Between (284.15 and 323.15) K and NRTL Interaction Parameters
• Surface Tensions of the Ternary Mixtures Containing an Isomeric Butanol + n-Hexane + 1-Chlorobutane at 298.15 K
• Solubilities of Ibuprofen in Different Pure Solvents
• Solubility of Genistein in Water, Methanol, Ethanol, Propan-2-ol, 1-Butanol, and Ethyl Acetate from (280 to 333) K
• Solubility of Andrographolide in Various Solvents from (288.2 to 323.2) K
• Solubilities of 2,4-Dinitro-l-phenylalanine in Monosolvents at (273.15 to 368.15) K
• Electrical Conductivity of Caprolactam Tetrabutylammonium Bromide Ionic Liquids in Aqueous and Alcohol Binary Systems
• Liquid-Liquid Equilibrium in Systems with an Ionic Liquid: Experimental Data for an Example of the Biphasic Acid Scavenging Utilizing Ionic Liquids Process
• 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
• Densities, Speeds of Sound, Excess Molar Volumes, and Excess Isentropic Compressibilities at T = (298.15 and 308.15) K for Methyl Methacrylate + 1-Alkanols (1-Butanol, 1-Pentanol, and 1-Heptanol) + Cyclohexane, + Benzene, + Toluene, + p-Xylene, and + Ethylbenzene
• Volumetric Behavior of Carbon Dioxide + Butan-1-ol Mixtures at 313.15 K
• Experimental Measurements and Correlations of Liquid-Liquid Equilibria for the Ternary and Quaternary Mixtures Formed by Dialkyl Carbonates at T = 298.15 K
• 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
• Solubilities of 3-Carboxy-3-hydroxypentanedioic Acid in Ethanol, Butan-1-ol, Water, Acetone, and Methylbenzene
• 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
• Measurement and Study on the Liquid Liquid Equilibrium of Ionic Liquids with Aliphatic Alcohols
• Solubility of Minoxidil in Methanol, Ethanol, 1-Propanol, 2-Propanol, 1-Butanol, and Water from (278.15 to 333.15) K
• Densities, Viscosities, and Speeds of Sound of Binary Liquid Mixtures of Ethylenediamine with Alcohols at T = (293.15 to 313.15) K
• Solubility of CO2 in Alcohols, Glycols, Ethers, and Ketones at High Pressures from (288.15 to 318.15) K
• Isothermal Vapor-Liquid Equilibrium of (1-Butanol + 1,8-Cineole) at 10 Temperatures between (278.15 and 323.15) K
• Densities, Excess Molar Volumes, and Refractive Properties of the Binary Mixtures of the Amino Acid Ionic Liquid [bmim][Gly] with 1-Butanol or Isopropanol at T = (298.15 to 313.15) K
• Measurement and Correlation of Solubility of Clopidogrel Hydrogen Sulfate (Metastable Form) in Lower Alcohols
• Liquid-Liquid Equilibria of Water + 3-Hydroxy-2-butanone + 1-Butanol
• Activity Coefficients at Infinite Dilution of Organic Compounds in Four New Imidazolium-Based Ionic Liquids
• 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
• 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
• Liquid Liquid Phase Behavior of Solutions of 1-Butyl-3-methylimidazolium Bis((trifluoromethyl)sulfonyl)amide (C4mimNTf2) in n-Alkyl Alcohols
• Isobaric Vapor Liquid Equilibria for the 1-Propanol + Ethylene Glycol Monopropyl Ether and 1-Butanol + Ethylene Glycol Monopropyl Ether Systems
• Vapor-Liquid Equilibria of Binary Mixtures Containing 1-Butanol and Hydrocarbons at 313.15 K
• Isobaric vapor liquid equilibium for the binary systerms of 1-butanol with o-xylene, m-xylene, p-xylene, and ethylbenzene at 101.33 kPa
• 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
• 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
• Solid Liquid Phase Equilibrium and Solubility of Dibenzo[b,d]furan and 9H-Fluoren-9-one in Organic Solvents
• Liquid Phase Behavior of 1-Butyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide with 1-Butanol or Hexan-1-ol: Measurements of Coexistence Curves, Density, and Interfacial Tension
• Solubility of 6-Chloropyridazin-3-amine in Different Solvents
• 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
• 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
• Biomass-Derived Platform Chemicals: Thermodynamic Studies on the Extraction of 5-Hydroxymethylfurfural from Ionic Liquids
• 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
• Vapor Liquid Equilibria, Excess Enthalpy, and Excess Volume of Binary Mixtures Containing an Alcohol (1-Butanol, 2-Butanol, or 2-Methyl-2-butanol) and 2-Ethoxy-2-methylbutane
• Liquid Liquid Phase Equilibria of the Binary Ionic Liquid Systems [Cn MIM][NTf2] + n-Butanol, + n-Pentanol, + H2O Using UV Spectroscopic and Densimetric Analytical Methods
• 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
• Vapor Liquid Equilibrium at p/kPa = 101.3 of the Binary Mixtures of Ethenyl Acetate with Methanol and Butan-1-ol
• Vapor Liquid Liquid Equilibria Measurements for the Dehydration of Ethanol, Isopropanol, and n-Propanol via Azeotropic Distillation Using DIPE and Isooctane as Entrainers
• Determination and Correlation of Solubility of Tris(3-hydroxypropyl)phosphine Oxide in Selected Solvents
• Density, Viscosity, and Isobaric Heat Capacity of the Mixture (1-Butanol + 1-Hexene)
• Solubility of Veratric Acid in Eight Monosolvents and Ethanol + 1-Butanol at Various Temperatures
• Solubilities of 4-Amino-4?-nitrodiphenyl Sulfide in Six Organic Solvents from 287.45 K to 365.55 K
• Solubilities of Rutaecarpine in Twelve Organic Solvents from (283.2 to 323.2) K
• 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
• Thermodynamic and Spectroscopic Study of the Ternary System Dimethyladipate + Tetrahydrofuran +1-Butanol at T = (288.15 to 323.15) 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
• Liquid Liquid, Vapor Liquid, and Vapor Liquid Liquid Equilibrium Data for the Water n-Butanol Cyclohexane System at Atmospheric Pressure: Experimental Determination and Correlation
• Density and Viscosity of the Binary Systems Ethanol + Butan-1-ol, + Pentan-1-ol, + Heptan-1-ol, + Octan-1-ol, Nonan-1-ol, + Decan-1-ol at 0.1 MPa and Temperatures from 283.15 K to 313.15 K
• 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
• Measurement and Correlation of Solubilities of Indole-2-carboxylic Acid in Ten Different Pure Solvents from (278.15 to 360.15) K
• Vapor Liquid Equilibrium for Several Compounds Relevant to the Biofuels Industry Modeled with the Wilson Equation
• Measurement and Correlation of Solubility of Azithromycin Monohydrate in Five Pure Solvents
• Densities and Viscosities of Diaminotoluene with Water, Ethanol, Propan-1-ol, and Butan-1-ol from (293.15 to 333.15) K
• Thermodynamics of Fluconazole Solubility in Various Solvents at Different Temperatures
• Densities, Refractive Indices, Viscosities, and Spectroscopic Study of 1-Amino-2-propanol + 1-Butanol and + 2-Butanol Solutions at (288.15 to 333.15) K
• Solubility of Dichloronitrobenzene in Eight Organic Solvents from T = (278.15 to 303.15) K: Measurement and Thermodynamic Modeling
• Phase Equilibrium (VLE, LLE, and VLLE) Data of the Ternary System: Ionic Liquid [OMIM][PF6] + Butan-1-ol + Butyl Acetate
• Infinite Dilution Activity Coefficients of Solutes Dissolved in Two Trihexyl(tetradecyl)phosphonium Ionic Liquids
• Determination and Correlation of Solubility Data and Dissolution Thermodynamic Data of Cefixime Trihydrate in Seven Pure Solvents
• Vapor Liquid Equilibrium Data for 1-Methyl-2-Pyrrolidone + (1-Butanol or 1-Hexene or Water) Binary Mixtures
• Solubility of Bioactive Compound Hesperidin in Six Pure Solvents at (298.15 to 333.15) K
• 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
• Thermodynamic Models for Determination of the Solubility of Dibenzothiophene in Different Solvents at Temperatures from (278.15 to 328.15) K
• Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
• Solubilities of Adipic Acid and Succinic Acid in Glutaric Acid + Acetone or n-butanol Mixture
• Ternary Liquid Liquid Equilibrium Data for the Water + Acetonitrile + {Butan-1-ol or 2-Methylpropan-1-ol} Systems at (303.2, 323.2, 343.2) K and 1 atm
• Vapor Liquid Equilibria Measurements for the Nine n-Alkane/Ketone Pairs Comprising 2-, 3-, and 4-Heptanone with n-Octane, n-Nonane, and n-Decane
• Speed of sound, density and related thermodynamic excess properties of binary mixtures of butan-2-one with C1-C4 nalkanols and chloroform
• Densities, Viscosities and Refractive Indices of the Ternary Mixture Dimethyladipate + 2-Butanone + 1-Butanol at T = (288.15 to 323.15) K
• Solubility and Thermodynamic Properties of (2S)-Pyrrolidine-2-carboxylic Acid in Water, Alcohols, and Water Alcohol Mixtures
• Measurement and Correlation of the Solubility of Penicillin V potassium in Ethanol + Water and 1-Butyl alcohol + Water Systems
• Thermodynamic Properties of Polymorphs of 2,2'-Thiodiethylene Bis[3-(3,5-di-tert-butyl-4-hydroxyphenyl)propionate]
• Solubilities of Naringin and Naringenin in Different Solvents and Dissociation Constants of Naringenin
• P ? T Data for 1-Butanol and Isobutyl Alcohol from (283.15 to 363.15) K at Pressures up to 66 MPa
• 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
• Solubility Determination and Thermodynamic Models for 2-Methylnaphthalene in Different Solvents from T = (278.15 to 303.15) K
• Measurement and Correlation of the Solubility for 4,4'-Diaminodiphenylmethane in Different Solvents
• Deduction of Physicochemical Properties from Solubilities: 2,4-Dihydroxybenzophenone, Biotin, and Caprolactam as Examples
• 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
• Vapor-Liquid Equilibrium Behaviors of Vanillin in 1-Butanol, 2-Butanol, and 2-Methyl-1-propanol
• Solubilities of Betulin in Fourteen Organic Solvents at Different Temperatures
• 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
• Solubility of Fluorene in Different Solvents from 278.98 K to 338.35 K
• Solubility of Triethylenediamine in Methanol, Ethanol, Isopropanol, I-Butanol, and Ethyl Acetate between 276.15 K and 363.15 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
• Study of the Temperature Dependence of Surface Tensions of Some Alkanol + Hexane Mixtures
• Measurements of Compressed Liquid Densities for CO2 (1) + Butan-1-ol (2) via a Vibrating Tube Densimeter at Temperatures from (313 to 363) K and Pressures up to 25 MPa
• Liquid-Liquid Equilibrium for the Quaternary System Water + Tetrahydrofuran + Toluene + 1-Butanol Mixture at 25 deg C and Atmospheric Pressure
• Thermodynamic Properties of 1-Butyl-3-methylpyridinium Tetrafluoroborate and Its Mixtures with Water and Alkanols
• Solubility of Oleanolic Acid in Various Solvents from (288.3 to 328.3) K
• Vapor-Liquid Equilibrium Behaviors of 3-Ethoxy-4-hydroxybenzaldehyde in Alcohol
• Solubility of Acenaphthylene in Different Solvents between (278 and 323) K
• Phase Equilibrium for the Esterification Reaction of Acetic Acid + Butan-1-ol at 101.3 kPa
• 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
• Densities, Excess Molar Volumes, and Isobaric Thermal Expansibilities for 1,2-Ethanediol + 1-Butanol, or 1-Hexanol, or 1-Octanol in the Temperature Range from (293.15 to 313.15) 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
• Vapor Liquid Equilibrium Behaviors of 5-Methyl-2-(1-methylethyl)phenol in Alcohol
• Refractive Indices and Deviations in Refractive Indices for Binary Mixtures of Formamide + 1-Butanol, + 2-Butanol, + 1,3-Butanediol, and + 1,4-Butanediol at Temperatures from (293.15 to 318.15) K
• Temperature and Composition Dependence of the Densities, Viscosities, and Speeds of Sound of Binary Liquid Mixtures of 1-Butanol with Hexadecane and Squalane
• Solubility of Hesperetin in Various Solvents from (288.2 to 323.2) K
• Isobaric Vapor-Liquid Equilibria for Tetrahydropyran and Alcohol Systems
• Determination and Correlation of Excess Molar Enthalpies of Eight Binary Systems Containing Acetophenone at Different Temperatures
• 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
• 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
• Solubilities of 1,4-Naphthoquinone in Acetone, Toluene, Xylene, Ethanol, and n-Butyl Alcohol
• 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
• Excess Enthalpy, Density, and Speed of Sound for the Ternary Mixture Methyl tert-Butyl Ether (1) + Butan-1-ol (2) + Octane (3)
• Vapor-Liquid Equilibrium for 1-Butanol + 1-Butene at (318.4 and 364.5) K and Vapor-Liquid Equilibrium of 1-Butanol + 2-Methylpropane, + n-Butane and 1-Butene + 2-Methylpropane at 318.4 K
• Solubility of D(-)-p-Hydroxyphenylglycine Dane Salt in Eight Alcohols between (293 and 343) K
• Measurement and Correlation of the Solubilities of m-Phthalic Acid in Monobasic Alcohols
• Solubility of Bis(benzoxazolyl-2-methyl) Sulfide in Different Pure Solvents and Ethanol + Water Binary Mixtures between (273.25 and 325.25) K
• 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 Diphenyl Carbonate in Pure Alcohols from (283 to 333) K
• Phase Equilibria Study of the Binary Systems (N-Butyl-4-methylpyridinium Tosylate Ionic Liquid + Organic Solvent, or Water)
• 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
• Solubility of Indinavir Sulfate in Different Solvents from (278.35 to 314.15) K
• Solubility of Podophyllotoxin in Six Organic Solvents from (283.2 to 323.2) K
• Excess Enthalpies of Binary and Ternary Mixtures Containing Dibutyl Ether, Cyclohexane, and 1-Butanol at 298.15 K
• Activity Coefficients at Infinite Dilution of Organic Compounds in Trihexyl(tetradecyl)phosphonium Bis(trifluoromethylsulfonyl)imide Using Inverse Gas Chromatography
• Liquid-Liquid Equilibria for Systems of 1-Butanol + Water + 2,6-Diaminopyridine and 1-Butanol + Water + 2-Aminopyridine
• Paramagnetic Ionic Liquid 1-Butyl-3-methylimidazolium Tetrabromidocobaltate(II): Activity Coefficients at Infinite Dilution of Organic Solutes and Crystal Structure
• Excess Molar Enthalpies of Five Binary Systems Containing Ethyl Acetoacetate at Different Temperatures
• Densities and Viscosities of Binary Mixtures of Cyclopropanecarboxylic Acid with Methanol, Ethanol, Propan-1-ol, and Butan-1-ol at Different Temperatures
• Densities, Viscosities, and Excess Molar Enthalpies of 2-Pyrrolidone + Butanol Isomers at T ) (293.15, 298.15, and 303.15) 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 of Thiotriazinone in Ethanol, 1-Propanol, 2-Propanol, 1-Butanol, Acetonitrile, Acetone, Ethyl Acetate, and Water from 293 K to 343 K
• Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
• Solubilities of 3-Pentadecylphenol in Ethanol, 1-Butanol, Toluene, Acetone, Tetrachloromethane, and Ethyl Acetate
• Apparent Molal Volumes and Viscosity B-Coefficients of Acetyl Salicylic Acid (2-Acetoxy Benzoic Acid) Solutions in Higher Alcohols at Different Temperatures
• Densities and Viscosities of exo-Tetrahydrodicyclopentadiene + n-Butanol and exo-Tetrahydrodicyclopentadiene + n-Pentanol at Temperatures of (293.15 to 313.15) K
• Measurement and Correlation of Solubilities of Decanedioic Acid in C4-C6 Alcohol Solvents
• Solubility of Phenanthrene in Binary Mixtures of C1-C4 Alcohols at 298.2 K
• Isobaric Vapor-Liquid Equilibria of Heptane + 1-Butanol and Heptane + 1-Pentanol Systems at (53.3 and 91.3) kPa
• Activity Coefficients at Infinite Dilution of Polar Solutes in 1-(2-Hydroxyethyl)-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Densities and Viscosities of Binary Mixtures of n-Butanol with 2-Butanol, Isobutanol, and tert-Butanol from (303.15 to 343.15) K
• 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
• Study of Ether-, Alcohol-, or Cyano-Functionalized Ionic Liquids Using Inverse Gas 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
• 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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