Chemical Properties of Acetone (CAS 67-64-1)

InChI

InChI=1S/C3H6O/c1-3(2)4/h1-2H3

InChI Key

CSCPPACGZOOCGX-UHFFFAOYSA-N

Formula

C3H6O

SMILES

CC(C)=O

Molecular Weight¹

58.08

CAS

67-64-1

Other Names

• (CH3)2CO
• 2-PROPANONE
• Chevron acetone
• DIMETHYL KETONE
• Dimethylformaldehyde
• Dimethylketal
• KETONE PROPANE
• Ketone, dimethyl-
• Methyl ketone
• NSC 135802
• Propan-2-one
• Propanone
• Pyroacetic ether
• Rcra waste number U002
• Sasetone
• UN 1090
• «beta»-Ketopropane
• «beta»-Ketopropane

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• T_ig : Autoignition Temperature (K).
• BasG : Gas basicity (kJ/mol).
• Δ_cH°_gas : Standard gas enthalpy of combustion (kJ/mol).
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• C_p,solid : Solid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• EA : Electron affinity (eV).
• LFL : Lower Flammability Limit (% in Air).
• UFL : Upper Flammability Limit (% in Air).
• T_flash,cc : Flash Point (Closed Cup Method) (K).
• T_flash,oc : Flash Point (Open Cup Method) (K).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• R_g : Radius of Gyration.
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_c : Critical 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°_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_boilr : Boiling point at reduced 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	0.3040		KDB
PAff	[811.50; 815.20]	kJ/mol
PAff	812.00	kJ/mol	NIST
PAff	815.20	kJ/mol	NIST
PAff	814.30	kJ/mol	NIST
PAff	812.60 ± 0.20	kJ/mol	NIST
PAff	811.50 ± 3.40	kJ/mol	NIST
PAff	811.50 ± 3.40	kJ/mol	NIST
Tig	738.15	K	KDB
BasG	[782.00; 784.70]	kJ/mol
BasG	782.10	kJ/mol	NIST
BasG	Outlier 784.70	kJ/mol	NIST
BasG	782.20	kJ/mol	NIST
BasG	782.00 ± 0.20	kJ/mol	NIST
BasG	782.10 ± 1.50	kJ/mol	NIST
BasG	782.10 ± 1.50	kJ/mol	NIST
ΔcH°gas	-1821.40 ± 0.84	kJ/mol	NIST
ΔcH°liquid	[-1804.20; -1772.00]	kJ/mol
ΔcH°liquid	-1772.00	kJ/mol	NIST
ΔcH°liquid	-1804.20	kJ/mol	NIST
μ	2.90	debye	KDB
η	[0.0003000; 0.0003121]	Pa×s
η	0.0003121	Pa×s	Densities and Viscosities of Binary Liquid Mixtures of Trichloroethylene and Tetrachloroethylene with Some Polar and Nonpolar Solvents
η	0.0003000	Pa×s	Densities and Viscosities of 1-Butyl-3-methylimidazolium Tetrafluoroborate + Molecular Solvent Binary Mixtures
EA	0.00	eV	NIST
LFL	2.60	% in Air	KDB
UFL	12.80	% in Air	KDB
Tflash,cc	257.59	K	KDB
Tflash,oc	255.37	K	KDB
ΔfG°	-153.20	kJ/mol	KDB
Rg	2.7400		KDB
ΔfH°gas	[-218.50; -216.40]	kJ/mol
ΔfH°gas	-217.70	kJ/mol	KDB
ΔfH°gas	-218.50 ± 0.59	kJ/mol	NIST
ΔfH°gas	-217.10 ± 0.50	kJ/mol	NIST
ΔfH°gas	-217.50 ± 0.67	kJ/mol	NIST
ΔfH°gas	-216.40	kJ/mol	NIST
ΔfH°liquid	-249.40 ± 0.63	kJ/mol	NIST
ΔfusH°	5.12	kJ/mol	Joback Calculated Property
ΔvapH°	[29.70; 31.30]	kJ/mol
ΔvapH°	31.27	kJ/mol	NIST
ΔvapH°	31.30	kJ/mol	NIST
ΔvapH°	29.70 ± 0.00	kJ/mol	NIST
IE	[9.50; 9.80]	eV
IE	9.70 ± 0.01	eV	NIST
IE	9.70	eV	NIST
IE	9.69 ± 0.01	eV	NIST
IE	9.68	eV	NIST
IE	9.71 ± 0.01	eV	NIST
IE	9.71 ± 0.03	eV	NIST
IE	9.71 ± 0.01	eV	NIST
IE	9.71	eV	NIST
IE	9.71	eV	NIST
IE	9.70 ± 0.00	eV	NIST
IE	9.71	eV	NIST
IE	9.71 ± 0.01	eV	NIST
IE	9.75 ± 0.03	eV	NIST
IE	9.72	eV	NIST
IE	9.74	eV	NIST
IE	9.71 ± 0.01	eV	NIST
IE	9.74 ± 0.03	eV	NIST
IE	9.68	eV	NIST
IE	9.71 ± 0.01	eV	NIST
IE	9.70 ± 0.10	eV	NIST
IE	9.68 ± 0.02	eV	NIST
IE	9.67	eV	NIST
IE	9.71 ± 0.03	eV	NIST
IE	9.71 ± 0.03	eV	NIST
IE	9.69 ± 0.01	eV	NIST
IE	9.71	eV	NIST
IE	Outlier 9.80	eV	NIST
IE	9.72	eV	NIST
IE	9.68	eV	NIST
IE	9.71 ± 0.02	eV	NIST
IE	Outlier 9.50	eV	NIST
IE	9.70	eV	NIST
IE	9.71	eV	NIST
IE	9.71	eV	NIST
IE	9.72	eV	NIST
log10WS	0.57		Relay (1.0) Calculated Property
logPoct/wat	0.595		Crippen Calculated Property
McVol	54.700	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
NFPA Health	1		KDB
Pc	4700.00	kPa	KDB
ρc	[234.06; 278.20]	kg/m3
ρc	268.91 ± 2.90	kg/m3	NIST
ρc	234.06 ± 1.51	kg/m3	NIST
ρc	278.20 ± 9.87	kg/m3	NIST
ρc	272.97 ± 1.16	kg/m3	NIST
ρc	252.06 ± 1.74	kg/m3	NIST
Inp	[437.00; 512.00]
Inp	470.23		NIST
Inp	470.90		NIST
Inp	470.70		NIST
Inp	470.10		NIST
Inp	469.67		NIST
Inp	469.50		NIST
Inp	469.28		NIST
Inp	469.41		NIST
Inp	470.00		NIST
Inp	470.00		NIST
Inp	469.00		NIST
Inp	469.00		NIST
Inp	481.00		NIST
Inp	484.00		NIST
Inp	477.00		NIST
Inp	478.00		NIST
Inp	488.70		NIST
Inp	488.20		NIST
Inp	485.00		NIST
Inp	497.00		NIST
Inp	475.00		NIST
Inp	Outlier 437.00		NIST
Inp	Outlier 437.00		NIST
Inp	450.00		NIST
Inp	443.50		NIST
Inp	465.00		NIST
Inp	441.00		NIST
Inp	444.00		NIST
Inp	Outlier 439.00		NIST
Inp	459.00		NIST
Inp	443.00		NIST
Inp	472.00		NIST
Inp	450.00		NIST
Inp	475.00		NIST
Inp	450.00		NIST
Inp	447.00		NIST
Inp	Outlier 439.00		NIST
Inp	503.00		NIST
Inp	477.55		NIST
Inp	Outlier 510.00		NIST
Inp	470.00		NIST
Inp	503.00		NIST
Inp	500.00		NIST
Inp	475.30		NIST
Inp	481.00		NIST
Inp	481.00		NIST
Inp	500.00		NIST
Inp	488.60		NIST
Inp	471.00		NIST
Inp	474.00		NIST
Inp	468.00		NIST
Inp	466.00		NIST
Inp	471.00		NIST
Inp	480.00		NIST
Inp	472.00		NIST
Inp	473.00		NIST
Inp	472.00		NIST
Inp	470.00		NIST
Inp	466.00		NIST
Inp	468.00		NIST
Inp	466.00		NIST
Inp	479.00		NIST
Inp	500.00		NIST
Inp	496.00		NIST
Inp	496.00		NIST
Inp	472.00		NIST
Inp	502.00		NIST
Inp	502.00		NIST
Inp	487.00		NIST
Inp	476.60		NIST
Inp	503.00		NIST
Inp	500.00		NIST
Inp	487.00		NIST
Inp	474.00		NIST
Inp	474.00		NIST
Inp	500.00		NIST
Inp	509.00		NIST
Inp	Outlier 512.00		NIST
Inp	459.00		NIST
Inp	471.00		NIST
Inp	450.00		NIST
Inp	476.00		NIST
Inp	501.00		NIST
Inp	470.00		NIST
Inp	470.00		NIST
Inp	450.00		NIST
Inp	497.00		NIST
Inp	472.00		NIST
Inp	500.00		NIST
Inp	460.00		NIST
Inp	473.00		NIST
Inp	473.00		NIST
Inp	473.00		NIST
Inp	465.00		NIST
Inp	460.00		NIST
Inp	469.00		NIST
Inp	491.00		NIST
Inp	474.00		NIST
Inp	484.00		NIST
Inp	468.00		NIST
Inp	469.00		NIST
Inp	478.00		NIST
Inp	468.00		NIST
Inp	503.00		NIST
Inp	500.00		NIST
Inp	471.00		NIST
Inp	470.00		NIST
Inp	479.00		NIST
Inp	502.00		NIST
Inp	477.55		NIST
Inp	470.23		NIST
Inp	469.50		NIST
Inp	469.00		NIST
Inp	478.00		NIST
Inp	475.00		NIST
Inp	465.00		NIST
Inp	443.00		NIST
Inp	447.00		NIST
I	[775.00; 854.00]
I	843.50		NIST
I	835.00		NIST
I	837.50		NIST
I	840.80		NIST
I	832.00		NIST
I	Outlier 847.00		NIST
I	Outlier 785.00		NIST
I	842.00		NIST
I	824.00		NIST
I	821.00		NIST
I	813.00		NIST
I	814.00		NIST
I	814.00		NIST
I	814.00		NIST
I	820.00		NIST
I	818.00		NIST
I	794.00		NIST
I	809.00		NIST
I	813.00		NIST
I	834.00		NIST
I	842.00		NIST
I	814.00		NIST
I	821.30		NIST
I	814.00		NIST
I	802.00		NIST
I	813.00		NIST
I	818.00		NIST
I	811.00		NIST
I	816.00		NIST
I	822.00		NIST
I	813.00		NIST
I	814.00		NIST
I	819.00		NIST
I	813.00		NIST
I	812.00		NIST
I	830.00		NIST
I	808.00		NIST
I	808.00		NIST
I	834.00		NIST
I	832.00		NIST
I	841.00		NIST
I	821.00		NIST
I	812.00		NIST
I	811.00		NIST
I	823.00		NIST
I	820.00		NIST
I	810.00		NIST
I	827.00		NIST
I	827.00		NIST
I	828.00		NIST
I	825.00		NIST
I	811.00		NIST
I	816.00		NIST
I	820.00		NIST
I	816.00		NIST
I	832.00		NIST
I	814.00		NIST
I	845.00		NIST
I	798.00		NIST
I	825.00		NIST
I	814.00		NIST
I	823.00		NIST
I	821.00		NIST
I	846.00		NIST
I	805.00		NIST
I	820.00		NIST
I	810.00		NIST
I	810.00		NIST
I	822.00		NIST
I	810.00		NIST
I	822.00		NIST
I	Outlier 854.00		NIST
I	816.00		NIST
I	800.00		NIST
I	818.00		NIST
I	845.00		NIST
I	814.00		NIST
I	814.00		NIST
I	Outlier 775.00		NIST
I	821.00		NIST
I	841.00		NIST
I	836.00		NIST
I	816.00		NIST
I	813.00		NIST
I	815.00		NIST
I	814.00		NIST
I	819.00		NIST
I	Outlier 788.00		NIST
I	823.00		NIST
I	Outlier 847.00		NIST
I	835.00		NIST
I	810.00		NIST
I	824.00		NIST
I	815.00		NIST
I	820.00		NIST
I	821.00		NIST
I	820.00		NIST
I	816.00		NIST
I	810.00		NIST
I	Outlier 847.00		NIST
I	819.00		NIST
I	810.00		NIST
I	813.00		NIST
I	830.00		NIST
I	809.00		NIST
I	821.30		NIST
I	811.00		NIST
I	794.00		NIST
S°liquid	[200.00; 220.50]	J/mol×K
S°liquid	200.40	J/mol×K	NIST
S°liquid	200.00	J/mol×K	NIST
S°liquid	220.50	J/mol×K	NIST
S°liquid	217.60	J/mol×K	NIST
Tboil	[323.40; 331.15]	K
Tboil	329.20	K	KDB
Tboil	329.30	K	Vapor-liquid equilibrium in the production of the ionic liquid, 1-hexyl-3-methylimidazolium bromide ([HMIm][Br]), in acetone
Tboil	329.26	K	Isobaric vapor-liquid equilibrium for acetone + methanol system containing different ionic liquids at 101.3 kPa
Tboil	329.56	K	Isobaric vapour-liquid equilibrium measurements and extractive distillation process for the azeotrope of (N,N-dimethylisopropylamine + acetone)
Tboil	329.33	K	Isobaric Vapor-Liquid Equilibrium Data for the Acetone + Hexamethyl Disiloxane + Ethyl Acetate Ternary System at 101.3 kPa: Determination and Correlation
Tboil	329.35	K	Isobaric Vapor-Liquid Equilibrium of Acetone + Methanol System in the Presence of Calcium Bromide
Tboil	329.27	K	Measurement of Isobaric Vapor - Liquid Equilibria of Dimethyl Carbonate with Acetone, 2-Butanone and 2-Pentanone at 101.3 kPa and Density and Speed of Sound at 298.15 K
Tboil	329.37	K	Vapor Liquid Equilibrium for the 1,1,1-Trifluorotrichloroethane + Sulfuryl Chloride System at 101.3 kPa
Tboil	329.20 ± 0.20	K	NIST
Tboil	329.30 ± 0.20	K	NIST
Tboil	329.45 ± 0.15	K	NIST
Tboil	329.45 ± 0.30	K	NIST
Tboil	329.00	K	NIST
Tboil	329.21 ± 0.04	K	NIST
Tboil	329.30	K	NIST
Tboil	329.45 ± 0.30	K	NIST
Tboil	329.40 ± 0.40	K	NIST
Tboil	329.25 ± 0.30	K	NIST
Tboil	329.47 ± 0.50	K	NIST
Tboil	329.23 ± 0.05	K	NIST
Tboil	329.25 ± 0.05	K	NIST
Tboil	329.26 ± 0.30	K	NIST
Tboil	329.00 ± 0.20	K	NIST
Tboil	329.30 ± 0.20	K	NIST
Tboil	329.30 ± 0.06	K	NIST
Tboil	329.25	K	NIST
Tboil	329.25 ± 0.15	K	NIST
Tboil	329.38 ± 0.30	K	NIST
Tboil	329.40 ± 0.20	K	NIST
Tboil	329.15 ± 0.30	K	NIST
Tboil	329.00 ± 1.00	K	NIST
Tboil	329.30 ± 0.20	K	NIST
Tboil	329.30 ± 0.30	K	NIST
Tboil	329.40 ± 0.40	K	NIST
Tboil	329.25 ± 0.50	K	NIST
Tboil	329.25 ± 0.30	K	NIST
Tboil	329.21 ± 0.10	K	NIST
Tboil	329.25 ± 0.30	K	NIST
Tboil	329.26 ± 0.30	K	NIST
Tboil	329.65 ± 1.00	K	NIST
Tboil	Outlier 330.95 ± 1.00	K	NIST
Tboil	329.25 ± 0.50	K	NIST
Tboil	329.26 ± 0.50	K	NIST
Tboil	329.15 ± 1.00	K	NIST
Tboil	Outlier 326.15 ± 1.00	K	NIST
Tboil	329.33 ± 0.20	K	NIST
Tboil	329.25 ± 1.00	K	NIST
Tboil	329.75 ± 1.00	K	NIST
Tboil	328.90 ± 0.40	K	NIST
Tboil	329.25 ± 0.50	K	NIST
Tboil	329.35 ± 1.00	K	NIST
Tboil	329.28 ± 0.15	K	NIST
Tboil	329.15 ± 1.00	K	NIST
Tboil	329.25 ± 0.50	K	NIST
Tboil	329.35 ± 0.50	K	NIST
Tboil	329.35 ± 0.50	K	NIST
Tboil	329.35 ± 0.50	K	NIST
Tboil	329.35 ± 0.20	K	NIST
Tboil	329.33 ± 0.20	K	NIST
Tboil	329.28 ± 0.30	K	NIST
Tboil	329.50 ± 0.50	K	NIST
Tboil	329.30 ± 0.50	K	NIST
Tboil	329.65 ± 0.50	K	NIST
Tboil	328.65 ± 1.00	K	NIST
Tboil	329.35 ± 0.50	K	NIST
Tboil	329.65 ± 1.00	K	NIST
Tboil	329.30 ± 0.50	K	NIST
Tboil	329.15 ± 1.00	K	NIST
Tboil	Outlier 323.40 ± 0.30	K	NIST
Tboil	329.27 ± 0.50	K	NIST
Tboil	329.30 ± 0.50	K	NIST
Tboil	329.40 ± 1.00	K	NIST
Tboil	329.25 ± 1.00	K	NIST
Tboil	330.15 ± 0.50	K	NIST
Tboil	329.75 ± 0.50	K	NIST
Tboil	329.25 ± 1.00	K	NIST
Tboil	329.65 ± 1.00	K	NIST
Tboil	329.20 ± 1.00	K	NIST
Tboil	329.15 ± 1.00	K	NIST
Tboil	329.26 ± 0.10	K	NIST
Tboil	Outlier 331.15 ± 3.00	K	NIST
Tboil	328.85 ± 1.00	K	NIST
Tboil	329.15 ± 2.00	K	NIST
Tboil	328.57 ± 1.00	K	NIST
Tboil	329.30 ± 1.00	K	NIST
Tboil	329.55 ± 1.00	K	NIST
Tboil	329.65 ± 0.30	K	NIST
Tboil	328.75 ± 1.00	K	NIST
Tboil	328.95 ± 1.00	K	NIST
Tboil	329.40 ± 0.20	K	NIST
Tboil	329.39 ± 0.50	K	NIST
Tboil	330.00 ± 1.00	K	NIST
Tboil	329.35 ± 0.30	K	NIST
Tboil	329.35 ± 0.30	K	NIST
Tboil	329.45 ± 1.00	K	NIST
Tboil	329.35 ± 0.30	K	NIST
Tboil	329.25 ± 0.20	K	NIST
Tboil	329.30 ± 0.40	K	NIST
Tboil	329.35 ± 0.20	K	NIST
Tboil	329.17 ± 0.20	K	NIST
Tboil	329.50 ± 0.50	K	NIST
Tboil	329.32 ± 0.30	K	NIST
Tboil	329.65 ± 1.00	K	NIST
Tboil	329.15 ± 1.00	K	NIST
Tboil	329.35 ± 1.00	K	NIST
Tboil	329.22 ± 0.20	K	NIST
Tboil	329.23 ± 0.10	K	NIST
Tboil	329.30 ± 1.00	K	NIST
Tboil	329.20 ± 0.30	K	NIST
Tboil	329.48 ± 1.00	K	NIST
Tboil	329.25 ± 1.00	K	NIST
Tboil	329.65 ± 1.00	K	NIST
Tboil	329.35 ± 1.00	K	NIST
Tboil	329.45 ± 0.50	K	NIST
Tboil	329.65 ± 1.00	K	NIST
Tboil	329.30 ± 0.30	K	NIST
Tboil	329.15 ± 1.00	K	NIST
Tboil	329.65 ± 1.00	K	NIST
Tboil	329.70 ± 1.50	K	NIST
Tboil	329.30 ± 0.50	K	NIST
Tboil	329.40 ± 1.00	K	NIST
Tboil	329.25 ± 0.30	K	NIST
Tboil	329.30 ± 0.50	K	NIST
Tboil	329.30 ± 1.00	K	NIST
Tboil	329.25 ± 0.30	K	NIST
Tboil	330.20 ± 1.00	K	NIST
Tboil	329.34 ± 0.50	K	NIST
Tboil	329.15 ± 1.00	K	NIST
Tboil	329.40 ± 1.00	K	NIST
Tboil	329.55 ± 1.00	K	NIST
Tboil	330.15 ± 1.00	K	NIST
Tboil	329.55 ± 1.00	K	NIST
Tboil	328.90 ± 1.00	K	NIST
Tboil	329.50 ± 1.00	K	NIST
Tboil	329.50 ± 0.50	K	NIST
Tboil	Outlier 330.85 ± 1.00	K	NIST
Tboil	329.45 ± 1.00	K	NIST
Tboil	329.45 ± 1.00	K	NIST
Tc	508.10	K	KDB
Tfus	178.30	K	KDB
Ttriple	[176.60; 178.50]	K
Ttriple	178.50 ± 0.30	K	NIST
Ttriple	176.60 ± 0.15	K	NIST
Ttriple	177.60 ± 0.30	K	NIST
Ttriple	177.60 ± 0.20	K	NIST
Vc	0.209	m3/kmol	KDB
Zc	0.2325190		KDB
Zra	0.25		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[80.58; 100.50]	J/mol×K	[332.60; 439.20]
Cp,gas	80.58 ± 0.81	J/mol×K	332.60	NIST
Cp,gas	80.96 ± 0.81	J/mol×K	334.00	NIST
Cp,gas	81.50 ± 0.16	J/mol×K	338.20	NIST
Cp,gas	83.35 ± 0.83	J/mol×K	347.80	NIST
Cp,gas	83.39 ± 0.83	J/mol×K	348.00	NIST
Cp,gas	87.03 ± 0.87	J/mol×K	363.00	NIST
Cp,gas	87.19 ± 0.17	J/mol×K	371.20	NIST
Cp,gas	87.53 ± 0.88	J/mol×K	372.30	NIST
Cp,gas	89.24 ± 0.89	J/mol×K	378.00	NIST
Cp,gas	91.84 ± 0.92	J/mol×K	393.00	NIST
Cp,gas	92.93 ± 0.19	J/mol×K	405.20	NIST
Cp,gas	94.18 ± 0.94	J/mol×K	408.00	NIST
Cp,gas	93.30	J/mol×K	410.00	NIST
Cp,gas	96.80 ± 1.90	J/mol×K	422.60	NIST
Cp,gas	99.40 ± 2.00	J/mol×K	428.00	NIST
Cp,gas	100.50 ± 2.00	J/mol×K	438.00	NIST
Cp,gas	98.66 ± 0.20	J/mol×K	439.20	NIST
Cp,liquid	[121.30; 133.90]	J/mol×K	[260.00; 302.40]
Cp,liquid	124.30	J/mol×K	260.00	NIST
Cp,liquid	121.30	J/mol×K	283.00	NIST
Cp,liquid	124.70	J/mol×K	289.40	NIST
Cp,liquid	126.30	J/mol×K	293.00	NIST
Cp,liquid	125.90	J/mol×K	293.20	NIST
Cp,liquid	124.68	J/mol×K	296.99	NIST
Cp,liquid	128.24	J/mol×K	298.00	NIST
Cp,liquid	124.70	J/mol×K	298.00	NIST
Cp,liquid	133.90	J/mol×K	298.00	NIST
Cp,liquid	124.70	J/mol×K	298.00	NIST
Cp,liquid	129.70	J/mol×K	298.00	NIST
Cp,liquid	125.45	J/mol×K	298.15	NIST
Cp,liquid	123.80	J/mol×K	298.15	NIST
Cp,liquid	123.80	J/mol×K	298.15	NIST
Cp,liquid	126.60	J/mol×K	298.15	NIST
Cp,liquid	126.60	J/mol×K	298.15	NIST
Cp,liquid	123.80	J/mol×K	298.15	NIST
Cp,liquid	125.90	J/mol×K	298.15	NIST
Cp,liquid	125.56	J/mol×K	298.20	NIST
Cp,liquid	123.80	J/mol×K	298.40	NIST
Cp,liquid	128.40	J/mol×K	302.40	NIST
Cp,solid	96.00	J/mol×K	173.00	NIST
η	[0.0002809; 0.0003849]	Pa×s	[278.15; 313.15]
η	0.0003849	Pa×s	278.15	Density and Viscosity of (2,2-Dichloro-N,N-di-2-propenylacetamide + Acetone) and (2,2-Dichloro-N,N-di-2-propenylacetamide + Ethanol) at T = (278.15 to 313.15) K
η	0.0003657	Pa×s	283.15	Density and Viscosity of (2,2-Dichloro-N,N-di-2-propenylacetamide + Acetone) and (2,2-Dichloro-N,N-di-2-propenylacetamide + Ethanol) at T = (278.15 to 313.15) K
η	0.0003511	Pa×s	288.15	Density and Viscosity of (2,2-Dichloro-N,N-di-2-propenylacetamide + Acetone) and (2,2-Dichloro-N,N-di-2-propenylacetamide + Ethanol) at T = (278.15 to 313.15) K
η	0.0003339	Pa×s	293.15	Density and Viscosity of (2,2-Dichloro-N,N-di-2-propenylacetamide + Acetone) and (2,2-Dichloro-N,N-di-2-propenylacetamide + Ethanol) at T = (278.15 to 313.15) K
η	0.0003200	Pa×s	293.15	Dynamic Viscosities of the Binary Systems Cyclohexane and Cyclopentane with Acetone, Butanone, or 2-Pentanone at Three Temperatures T ) (293.15, 298.15, and 303.15) K
η	0.0003200	Pa×s	293.15	Physical properties of the binary systems methylcyclopentane with ketones (acetone, butanone and 2-pentanone) at T = (293.15, 298.15, and 303.15) K. New UNIFAC-VISCO interaction parameters
η	0.0003060	Pa×s	298.15	Physical properties of the binary systems methylcyclopentane with ketones (acetone, butanone and 2-pentanone) at T = (293.15, 298.15, and 303.15) K. New UNIFAC-VISCO interaction parameters
η	0.0003212	Pa×s	298.15	Density and Viscosity of (2,2-Dichloro-N,N-di-2-propenylacetamide + Acetone) and (2,2-Dichloro-N,N-di-2-propenylacetamide + Ethanol) at T = (278.15 to 313.15) K
η	0.0003027	Pa×s	298.15	Excess parameter studies on the binary mixtures of toluene with ketones at different temperatures
η	0.0003060	Pa×s	298.15	Dynamic Viscosities of the Binary Systems Cyclohexane and Cyclopentane with Acetone, Butanone, or 2-Pentanone at Three Temperatures T ) (293.15, 298.15, and 303.15) K
η	0.0003027	Pa×s	298.15	Density and Viscosity of Ketones with Toluene at Different Temperatures and at Atmospheric Pressure
η	0.0002918	Pa×s	303.15	Density and Viscosity of Ketones with Toluene at Different Temperatures and at Atmospheric Pressure
η	0.0002920	Pa×s	303.15	Dynamic Viscosities of the Binary Systems Cyclohexane and Cyclopentane with Acetone, Butanone, or 2-Pentanone at Three Temperatures T ) (293.15, 298.15, and 303.15) K
η	0.0002918	Pa×s	303.15	Excess parameter studies on the binary mixtures of toluene with ketones at different temperatures
η	0.0002920	Pa×s	303.15	Physical properties of the binary systems methylcyclopentane with ketones (acetone, butanone and 2-pentanone) at T = (293.15, 298.15, and 303.15) K. New UNIFAC-VISCO interaction parameters
η	0.0003086	Pa×s	303.15	Density and Viscosity of (2,2-Dichloro-N,N-di-2-propenylacetamide + Acetone) and (2,2-Dichloro-N,N-di-2-propenylacetamide + Ethanol) at T = (278.15 to 313.15) K
η	0.0002809	Pa×s	308.15	Density and Viscosity of Ketones with Toluene at Different Temperatures and at Atmospheric Pressure
η	0.0002809	Pa×s	308.15	Excess parameter studies on the binary mixtures of toluene with ketones at different temperatures
η	0.0002939	Pa×s	308.15	Density and Viscosity of (2,2-Dichloro-N,N-di-2-propenylacetamide + Acetone) and (2,2-Dichloro-N,N-di-2-propenylacetamide + Ethanol) at T = (278.15 to 313.15) K
η	0.0002839	Pa×s	313.15	Density and Viscosity of (2,2-Dichloro-N,N-di-2-propenylacetamide + Acetone) and (2,2-Dichloro-N,N-di-2-propenylacetamide + Ethanol) at T = (278.15 to 313.15) K
ΔfusH	[4.77; 5.72]	kJ/mol	[176.60; 178.50]
ΔfusH	5.72	kJ/mol	176.60	NIST
ΔfusH	5.72	kJ/mol	176.60	NIST
ΔfusH	5.71	kJ/mol	176.62	NIST
ΔfusH	5.69	kJ/mol	177.60	NIST
ΔfusH	5.69	kJ/mol	177.60	NIST
ΔfusH	4.77	kJ/mol	178.50	NIST
ΔvapH	[9.20; 35.00]	kJ/mol	[210.50; 498.00]
ΔvapH	32.90	kJ/mol	210.50	NIST
ΔvapH	33.80	kJ/mol	236.00	NIST
ΔvapH	30.70	kJ/mol	271.50	NIST
ΔvapH	32.10	kJ/mol	271.50	NIST
ΔvapH	35.00	kJ/mol	271.50	NIST
ΔvapH	32.60	kJ/mol	285.50	NIST
ΔvapH	32.70	kJ/mol	294.50	NIST
ΔvapH	32.80	kJ/mol	305.00	NIST
ΔvapH	31.90	kJ/mol	307.00	NIST
ΔvapH	32.10	kJ/mol	308.00	NIST
ΔvapH	31.80	kJ/mol	319.00	NIST
ΔvapH	31.10	kJ/mol	319.50	NIST
ΔvapH	29.10	kJ/mol	329.30	NIST
ΔvapH	29.12	kJ/mol	329.40	KDB
ΔvapH	29.09	kJ/mol	338.00	NIST
ΔvapH	30.60	kJ/mol	351.00	NIST
ΔvapH	26.10	kJ/mol	373.00	NIST
ΔvapH	29.90	kJ/mol	408.50	NIST
ΔvapH	29.50	kJ/mol	419.00	NIST
ΔvapH	21.70	kJ/mol	423.00	NIST
ΔvapH	15.30	kJ/mol	473.00	NIST
ΔvapH	29.70	kJ/mol	482.50	NIST
ΔvapH	9.20	kJ/mol	498.00	NIST
Pvap	[30.23; 302.56]	kPa	[297.66; 365.43]
Pvap	30.23	kPa	297.66	Vapor-Liquid Equilibrium for Binary Systems of Diacetyl with Methanol and Acetone
Pvap	30.23	kPa	297.67	Vapor Liquid Equilibrium for Binary Systems of 2,3-Pentanedione with Diacetyl and Acetone
Pvap	35.22	kPa	301.25	Vapor Liquid Equilibrium for Binary Systems of 2,3-Pentanedione with Diacetyl and Acetone
Pvap	35.22	kPa	301.25	Vapor-Liquid Equilibrium for Binary Systems of Diacetyl with Methanol and Acetone
Pvap	38.04	kPa	303.15	Vapor-Liquid Equilibrium for Binary Systems of Diacetyl with Methanol and Acetone
Pvap	40.00	kPa	304.37	Vapor-Liquid Equilibrium for Binary Systems of Diacetyl with Methanol and Acetone
Pvap	45.21	kPa	307.33	Vapor Liquid Equilibrium for Binary Systems of 2,3-Pentanedione with Diacetyl and Acetone
Pvap	45.21	kPa	307.33	Vapor-Liquid Equilibrium for Binary Systems of Diacetyl with Methanol and Acetone
Pvap	50.40	kPa	310.08	Vapor Liquid Equilibrium for Binary Systems of 2,3-Pentanedione with Diacetyl and Acetone
Pvap	50.40	kPa	310.08	Vapor-Liquid Equilibrium for Binary Systems of Diacetyl with Methanol and Acetone
Pvap	55.29	kPa	312.52	Vapor Liquid Equilibrium for Binary Systems of 2,3-Pentanedione with Diacetyl and Acetone
Pvap	55.29	kPa	312.52	Vapor-Liquid Equilibrium for Binary Systems of Diacetyl with Methanol and Acetone
Pvap	56.64	kPa	313.15	Vapor-Liquid Equilibrium for Binary Systems of Diacetyl with Methanol and Acetone
Pvap	57.96	kPa	314.00	Isobaric vapor liquid equilibria for acetone + methanol + lithium nitrate at 100 kPa
Pvap	60.29	kPa	314.76	Vapor-Liquid Equilibrium for Binary Systems of Diacetyl with Methanol and Acetone
Pvap	60.29	kPa	314.76	Vapor Liquid Equilibrium for Binary Systems of 2,3-Pentanedione with Diacetyl and Acetone
Pvap	65.08	kPa	316.80	Vapor-Liquid Equilibrium for Binary Systems of Diacetyl with Methanol and Acetone
Pvap	65.08	kPa	316.80	Vapor Liquid Equilibrium for Binary Systems of 2,3-Pentanedione with Diacetyl and Acetone
Pvap	64.95	kPa	317.00	Isobaric vapor liquid equilibria for acetone + methanol + lithium nitrate at 100 kPa
Pvap	68.20	kPa	318.15	Isothermal Vapor-Liquid Equilibria for Binary Mixtures of Methyl Nonafluorobutyl Ether + Acetone, Cyclopentyl Methyl Ether, Ethyl Acetate, n-Heptane, Methanol, and Toluene
Pvap	70.07	kPa	318.77	Vapor-Liquid Equilibrium for Binary Systems of Diacetyl with Methanol and Acetone
Pvap	70.07	kPa	318.77	Vapor Liquid Equilibrium for Binary Systems of 2,3-Pentanedione with Diacetyl and Acetone
Pvap	72.60	kPa	320.00	Isobaric vapor liquid equilibria for acetone + methanol + lithium nitrate at 100 kPa
Pvap	80.96	kPa	323.00	Isobaric vapor liquid equilibria for acetone + methanol + lithium nitrate at 100 kPa
Pvap	81.65	kPa	323.15	Vapor-Liquid Equilibrium for Binary Systems of Diacetyl with Methanol and Acetone
Pvap	90.08	kPa	326.00	Isobaric vapor liquid equilibria for acetone + methanol + lithium nitrate at 100 kPa
Pvap	96.15	kPa	327.90	Vapor Liquid Equilibrium Data for Binary Mixtures of Acetic Acid + Anisole, Acetone + Anisole, and Isopropanol + Anisole at Pressure 96.15 kPa
Pvap	100.00	kPa	329.00	Influence of Some Ionic Liquids Containing the Trifluoromethanesulfonate Anion on the Vapor Liquid Equilibria of the Acetone + Methanol System
Pvap	100.00	kPa	329.00	Isobaric vapor liquid equilibria for acetone + methanol + lithium nitrate at 100 kPa
Pvap	100.00	kPa	329.00	1-Ethyl-3-methylimidazolium Dicyanamide as a Very Efficient Entrainer for the Extractive Distillation of the Acetone + Methanol System
Pvap	101.30	kPa	329.26	Isobaric vapor-liquid equilibrium for acetone + methanol system containing different ionic liquids at 101.3 kPa
Pvap	101.33	kPa	329.30	Vapor-liquid equilibrium in the production of the ionic liquid, 1-hexyl-3-methylimidazolium bromide ([HMIm][Br]), in acetone
Pvap	101.30	kPa	329.33	Isobaric Vapor-Liquid Equilibrium Data for the Acetone + Hexamethyl Disiloxane + Ethyl Acetate Ternary System at 101.3 kPa: Determination and Correlation
Pvap	101.00	kPa	329.35	Isobaric Vapor-Liquid Equilibrium of Acetone + Methanol System in the Presence of Calcium Bromide
Pvap	101.30	kPa	329.37	Vapor Liquid Equilibrium for the 1,1,1-Trifluorotrichloroethane + Sulfuryl Chloride System at 101.3 kPa
Pvap	101.30	kPa	329.56	Isobaric vapour-liquid equilibrium measurements and extractive distillation process for the azeotrope of (N,N-dimethylisopropylamine + acetone)
Pvap	110.78	kPa	332.00	Isobaric vapor liquid equilibria for acetone + methanol + lithium nitrate at 100 kPa
Pvap	115.70	kPa	333.15	Thermodynamics of binary mixtures of N-methyl-2-pyrrolidinone and ketone. Experimental results and modelling of the solid-liquid equilibrium and vapou-liquid equilibrium. The Modified UNIFAC (Do) model characterization
Pvap	122.47	kPa	335.00	Isobaric vapor liquid equilibria for acetone + methanol + lithium nitrate at 100 kPa
Pvap	135.11	kPa	338.00	Isobaric vapor liquid equilibria for acetone + methanol + lithium nitrate at 100 kPa
Pvap	297.10	kPa	364.51	Vapor Liquid Equilibrium for Six Binary Systems of C4-Hydrocarbons + 2-Propanone
Pvap	294.30	kPa	364.51	Vapor Liquid Equilibrium for Six Binary Systems of C4-Hydrocarbons + 2-Propanone
Pvap	296.40	kPa	364.51	Vapor Liquid Equilibrium for Six Binary Systems of C4-Hydrocarbons + 2-Propanone
Pvap	296.80	kPa	364.52	Vapor Liquid Equilibrium for Six Binary Systems of C4-Hydrocarbons + 2-Propanone
Pvap	302.56	kPa	365.43	Vapor Liquid Equilibrium for Six Binary Systems of C4-Hydrocarbons + 2-Propanone
n0	[1.34491; 1.36152]		[288.15; 318.15]
n0	1.36152		288.15	Densities, Refractive indices and Viscosities for Binary and Ternary Mixtures of Acetone, Ethanol and 2,2,4-Trimethylpentane at T = (288.15, 298.15, and 308.15) K
n0	1.36146		288.15	Density, Speed of Sound, and Refractive Index of 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate with Acetone, Methyl Acetate, and Ethyl Acetate at Temperatures from (278.15 to 328.15) K
n0	1.35900		293.15	Solubilities of (2,5-Dihydroxyphenyl)diphenyl Phosphine Oxide in Selected Solvents
n0	1.35880		293.15	Isothermal vapour-liquid equilibrium data for the binary systems 2-propanone + (2-butanol or propanoic acid)
n0	1.35900		293.15	Solubilities of 3,9-Dimethyl-3,9-dioxide-2,4,8,10-tetraoxa-3,9-diphosphaspiro[5.5]undecane in Selected Solvents
n0	1.35880		293.15	Solubilities of Methyldiphenylphosphine Oxide in Selected Solvents
n0	1.35900		293.15	Solubilities of 2-(6-Oxido-6H-dibenz[c,e][1,2]oxaphosphorin-6-yl)-1,4-dihydroxy Phenylene in the Selected Solvents
n0	1.35900		293.15	Solubilities of Phosphorus-Containing Compounds in Selected Solvents
n0	1.35900		293.15	Solubilities of Some Phosphaspirocyclic Compounds in Selected Solvents
n0	1.35890		293.15	Isothermal and Isobaric Vapor-Liquid Equilibria of the Ternary System of 2,2-Dimethoxypropane + Acetone + Methanol
n0	1.35860		293.15	Isobaric Vapor Liquid Equilibrium for Nine Binary Systems of Cracking C5 Fraction at 250 kPa
n0	1.35550		298.00	Quaternary and ternary LLE measurements for solvent (2-methyltetrahydrofuran and cyclopentyl methyl ether) + furfural + acetic acid + water between 298 and 343 K
n0	1.35600		298.15	Physical properties and their corresponding changes of mixing for the ternary mixture acetone + n-hexane +water at 298.15K
n0	1.35597		298.15	Isobaric vapor liquid equilibria for mixtures of acetone, ethanol, and 2,2,4-trimethylpentane at 101.3 kPa
n0	1.35732		298.15	Vapor liquid equilibria and interfacial tensions for the ternary system acetone + 2,2 -oxybis[propane] + cyclohexane and its constituent binary systems
n0	1.35553		298.15	Quaternary, Ternary and Binary LLE Measurements for 2-Methoxy-2-methylbutane + Furfural + Acetic Acid + Water at Temperatures between 298 and 341 K
n0	1.35553		298.15	Quaternary, Ternary, and Binary LLE Measurements for 2-Methoxy-2-methylpropane + Furfural + Acetic Acid + Water at Temperatures between 298 and 307 K
n0	1.35620		298.15	Solubility of a-Carotene in Binary Solvents Formed by Some Hydrocarbons with 2,5,8-Trioxanonane, 2-Propanone, and Cyclohexanone
n0	1.35553		298.15	Ternary and Binary LLE Measurements for Solvent (4- Methyl-2-pentanone and 2-Methyl-2-butanol) + Furfural + Water between 298 and 401 K
n0	1.35605		298.15	Densities, Refractive indices and Viscosities for Binary and Ternary Mixtures of Acetone, Ethanol and 2,2,4-Trimethylpentane at T = (288.15, 298.15, and 308.15) K
n0	1.35820		298.15	Isobaric Vapor Liquid Equilibria for Binary Systems of Acetone + Isopropenyl Acetate, 2-Butanone + Isopropenyl Acetate, and Isopropenyl Acetate + Acetylacetone at 101.3 kPa
n0	1.35550		298.15	Ternary and binary LLE measurements for solvent (2-methyltetrahydrofuran and cyclopentyl methyl ether) + furfural + water between 298 and 343 K
n0	1.35566		298.15	Properties of ionic liquid HMIMPF6 with carbonates, ketones and alkyl acetates
n0	1.35732		298.15	Phase equilibria and interfacial tensions in the systems methyl tert-butyl ether + acetone + cyclohexane, methyl tert-butyl ether + acetone and methyl tert-butyl ether + cyclohexane
n0	1.35597		298.15	Density, Speed of Sound, and Refractive Index of 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate with Acetone, Methyl Acetate, and Ethyl Acetate at Temperatures from (278.15 to 328.15) K
n0	1.35054		308.15	Density, Speed of Sound, and Refractive Index of 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate with Acetone, Methyl Acetate, and Ethyl Acetate at Temperatures from (278.15 to 328.15) K
n0	1.35057		308.15	Densities, Refractive indices and Viscosities for Binary and Ternary Mixtures of Acetone, Ethanol and 2,2,4-Trimethylpentane at T = (288.15, 298.15, and 308.15) K
n0	1.34491		318.15	Density, Speed of Sound, and Refractive Index of 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate with Acetone, Methyl Acetate, and Ethyl Acetate at Temperatures from (278.15 to 328.15) K
ρl	[755.31; 801.67]	kg/m3	[283.15; 323.14]
ρl	801.67	kg/m3	283.15	Experimental Densities and Excess Volumes for Binary Mixtures Containing Propionic Acid, Acetone and Water from 283.15 K to 323.15 K at Atmospheric Pressure
ρl	796.04	kg/m3	288.15	Experimental Densities and Excess Volumes for Binary Mixtures Containing Propionic Acid, Acetone and Water from 283.15 K to 323.15 K at Atmospheric Pressure
ρl	790.00	kg/m3	293.00	KDB
ρl	790.36	kg/m3	293.15	Experimental Densities and Excess Volumes for Binary Mixtures Containing Propionic Acid, Acetone and Water from 283.15 K to 323.15 K at Atmospheric Pressure
ρl	790.31	kg/m3	293.15	Excess Molar Enthalpies for Binary Mixtures of Ethanol + Acetone, + Octane, + Cyclohexane and 1-Propanol + Acetone, + Octane, + Heptane at 323.15
ρl	789.99	kg/m3	293.15	Thermodynamic properties of binary mixtures of the ionic liquid [emim][BF4] with acetone and dimethylsulphoxide
ρl	790.00	kg/m3	293.15	Thermophysical approach to understand the nature of molecular interactions and structural factor between methyl isobutyl ketone and organic solvents mixtures
ρl	790.19	kg/m3	293.15	Thermodynamics of amide + ketone mixtures. 1. Volumetric, speed of sound and refractive index data for N,N-dimethylformamide + 2-alkanone systems at several temperatures
ρl	784.50	kg/m3	293.15	(Vapour + liquid) equilibria for (2-ethoxypropene + acetone) and (2-ethoxypropene + butanone)
ρl	784.30	kg/m3	293.15	Liquid Liquid Equilibrium for the Ternary System Acetone Oxime Methyl Ether Acetone Water
ρl	790.21	kg/m3	293.15	(Liquid + liquid) equilibria for (water + 1-propanol or acetone + .beta.-citronellol) at different temperatures
ρl	790.66	kg/m3	293.20	Ionic liquid 1-hexyl-3-methylimidazolium hexafluorophosphate, an efficient solvent for extraction of acetone from aqueous solutions
ρl	784.64	kg/m3	298.15	Experimental Densities and Excess Volumes for Binary Mixtures Containing Propionic Acid, Acetone and Water from 283.15 K to 323.15 K at Atmospheric Pressure
ρl	785.10	kg/m3	298.15	Measurement and correlation of solubility and solution thermodynamics of 1,3-dimethylurea in different solvents from T = (288.15 to 328.15) K
ρl	784.30	kg/m3	298.15	Phase equilibrium study of binary and ternary mixtures of ionic liquids + acetone + methanol
ρl	784.39	kg/m3	298.15	Excess Molar Volumes and Surface Tensions of Xylene with Acetone or 2-Butanone at 298.15 K
ρl	785.09	kg/m3	298.15	Thermodynamics of ketone + amine mixtures. Part IX. Excess molar enthalpies at 298.15K for dipropylamine, or dibutylamine + 2-alkanone systems and modeling of linear or aromatic amine + 2-alkanone mixtures in terms of DISQUAC and ERAS
ρl	785.23	kg/m3	298.15	Separation of sulfur compounds from alkanes with 1-alkylcyanopyridinium-based ionic liquids
ρl	785.32	kg/m3	298.15	Effect of the alkyl side chain of the 1-alkylpiperidinium-based ionic liquids on desulfurization of fuels
ρl	785.32	kg/m3	298.15	Extraction desulfurization process of fuels with ionic liquids
ρl	783.80	kg/m3	298.15	Solubility and solution thermodynamics of sorbic acid in eight pure organic solvents
ρl	784.24	kg/m3	298.15	Apparent molar volumes and compressibilities of tetrabutyl-ammonium bromide in organic solvents
ρl	784.23	kg/m3	298.15	Density and speed of sound of lithium bromide with organic solvents: Measurement and correlation
ρl	785.23	kg/m3	298.15	Separation of pyridine from heptane with tricyanomethanide-based ionic liquids
ρl	784.41	kg/m3	298.15	Densities, viscosities, and refractive indices of binary and ternary mixtures of methanol, acetone, and chloroform at temperatures from (298.15-318.15) K and ambient pressure
ρl	784.65	kg/m3	298.15	Excess molar enthalpies and volumes of binary mixtures of nonafluorobutylmethylether with ketones at T = 298.15 K
ρl	783.81	kg/m3	298.15	Partial Molar Volumes of Butyltriethylammonium Iodide in Single Nonaqueous Solvents at 298.15 K
ρl	784.43	kg/m3	298.15	Thermodynamics of amide + ketone mixtures. 1. Volumetric, speed of sound and refractive index data for N,N-dimethylformamide + 2-alkanone systems at several temperatures
ρl	785.09	kg/m3	298.15	Thermodynamics of Ketone + Amine Mixtures. Part VIII. Molar Excess Enthalpies at 298.15 K for n-Alkanone + Aniline or + N-Methylaniline Systems
ρl	786.77	kg/m3	298.15	Separation of ethylbenzene/styrene systems using ionic liquids in ternary LLE
ρl	784.40	kg/m3	298.15	Thermodynamic properties of binary mixtures of the ionic liquid [emim][BF4] with acetone and dimethylsulphoxide
ρl	785.09	kg/m3	298.15	Thermodynamics of ketone + amine mixtures. Part X. Excess molarenthalpies at 298.15 K for N,N,N-triethylamine + 2-alkanone systems.Characterization of tertiary amine + 2-alkanone, and ofamino-ketone + n-alkane mixtures in terms of DISQUAC
ρl	784.10	kg/m3	298.15	Density, Speed of Sound, and Derived Thermodynamic Properties of Ionic Liquids [EMIM]+[BETI]- or ([EMIM]+[CH3(OCH2CH2)2OSO3]- + Methanol or + Acetone) at T = (298.15 or 303.15 or 313.15) K
ρl	785.00	kg/m3	298.15	Vapor Liquid Equilibrium Data for 2,3-Pentanedione + (Acetaldehyde or Acetone) at (100, 150, and 200) kPa
ρl	784.40	kg/m3	298.20	Ionic liquid 1-hexyl-3-methylimidazolium hexafluorophosphate, an efficient solvent for extraction of acetone from aqueous solutions
ρl	778.88	kg/m3	303.14	Experimental Densities and Excess Volumes for Binary Mixtures Containing Propionic Acid, Acetone and Water from 283.15 K to 323.15 K at Atmospheric Pressure
ρl	778.63	kg/m3	303.15	Thermodynamics of amide + ketone mixtures. 1. Volumetric, speed of sound and refractive index data for N,N-dimethylformamide + 2-alkanone systems at several temperatures
ρl	778.66	kg/m3	303.15	Densities, viscosities, and refractive indices of binary and ternary mixtures of methanol, acetone, and chloroform at temperatures from (298.15-318.15) K and ambient pressure
ρl	779.00	kg/m3	303.15	Thermophysical approach to understand the nature of molecular interactions and structural factor between methyl isobutyl ketone and organic solvents mixtures
ρl	778.40	kg/m3	303.15	Density, Speed of Sound, and Derived Thermodynamic Properties of Ionic Liquids [EMIM]+[BETI]- or ([EMIM]+[CH3(OCH2CH2)2OSO3]- + Methanol or + Acetone) at T = (298.15 or 303.15 or 313.15) K
ρl	778.87	kg/m3	303.15	Thermodynamic properties of binary mixtures of the ionic liquid [emim][BF4] with acetone and dimethylsulphoxide
ρl	778.70	kg/m3	303.20	Ionic liquid 1-hexyl-3-methylimidazolium hexafluorophosphate, an efficient solvent for extraction of acetone from aqueous solutions
ρl	773.07	kg/m3	308.15	Experimental Densities and Excess Volumes for Binary Mixtures Containing Propionic Acid, Acetone and Water from 283.15 K to 323.15 K at Atmospheric Pressure
ρl	773.08	kg/m3	308.15	Densities, viscosities, and refractive indices of binary and ternary mixtures of methanol, acetone, and chloroform at temperatures from (298.15-318.15) K and ambient pressure
ρl	773.07	kg/m3	308.15	Thermodynamic properties of binary mixtures of the ionic liquid [emim][BF4] with acetone and dimethylsulphoxide
ρl	767.21	kg/m3	313.14	Experimental Densities and Excess Volumes for Binary Mixtures Containing Propionic Acid, Acetone and Water from 283.15 K to 323.15 K at Atmospheric Pressure
ρl	767.00	kg/m3	313.15	Thermophysical approach to understand the nature of molecular interactions and structural factor between methyl isobutyl ketone and organic solvents mixtures
ρl	766.95	kg/m3	313.15	Densities, viscosities, and refractive indices of binary and ternary mixtures of methanol, acetone, and chloroform at temperatures from (298.15-318.15) K and ambient pressure
ρl	766.90	kg/m3	313.15	Density, Speed of Sound, and Derived Thermodynamic Properties of Ionic Liquids [EMIM]+[BETI]- or ([EMIM]+[CH3(OCH2CH2)2OSO3]- + Methanol or + Acetone) at T = (298.15 or 303.15 or 313.15) K
ρl	761.29	kg/m3	318.14	Experimental Densities and Excess Volumes for Binary Mixtures Containing Propionic Acid, Acetone and Water from 283.15 K to 323.15 K at Atmospheric Pressure
ρl	761.26	kg/m3	318.15	Densities, viscosities, and refractive indices of binary and ternary mixtures of methanol, acetone, and chloroform at temperatures from (298.15-318.15) K and ambient pressure
ρl	755.31	kg/m3	323.14	Experimental Densities and Excess Volumes for Binary Mixtures Containing Propionic Acid, Acetone and Water from 283.15 K to 323.15 K at Atmospheric Pressure
ΔfusS	[26.70; 32.36]	J/mol×K	[176.62; 178.50]
ΔfusS	32.36	J/mol×K	176.62	NIST
ΔfusS	32.00	J/mol×K	177.60	NIST
ΔfusS	32.03	J/mol×K	177.60	NIST
ΔfusS	26.70	J/mol×K	178.50	NIST
csound,fluid	1162.00	m/s	298.15	Vapor liquid equilibria for systems of diethyl carbonate and ketones and determination of group interaction parameters for the UNIFAC and ASOG methods
γ	[0.02; 0.02]	N/m	[287.81; 328.15]
γ	0.02	N/m	287.81	Surface Tension of Pure Liquids and Binary Liquid Mixtures
γ	0.02	N/m	288.15	Surface Tension of the Ternary System Water + Acetone + Toluene
γ	0.02	N/m	293.15	Investigation of Surface Properties and Solubility of 1-Vinyl-3-alkyl/Esterimidazolium Halide Ionic Liquids by Density Functional Methods
γ	0.02	N/m	297.82	Surface Tension of Pure Liquids and Binary Liquid Mixtures
γ	0.02	N/m	298.15	Surface Tension of the Ternary System Water + Acetone + Toluene
γ	0.02	N/m	298.20	KDB
γ	0.02	N/m	307.86	Surface Tension of Pure Liquids and Binary Liquid Mixtures
γ	0.02	N/m	308.15	Surface Tension of the Ternary System Water + Acetone + Toluene
γ	0.02	N/m	317.86	Surface Tension of Pure Liquids and Binary Liquid Mixtures
γ	0.02	N/m	318.15	Surface Tension of the Ternary System Water + Acetone + Toluene
γ	0.02	N/m	327.88	Surface Tension of Pure Liquids and Binary Liquid Mixtures
γ	0.02	N/m	328.15	Surface Tension of the Ternary System Water + Acetone + Toluene

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboilr	329.30	K	2.70	NIST

Datasets

1. Viscosity, Pa*s (1)
2. Speed of sound, m/s (2)

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
303.15	101.30	0.0003
Reference

Speed of sound, m/s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Speed of sound, m/s - Liquid
265.67	102.00	1298.93
265.67	504.00	1301.09
265.67	750.00	1302.5
265.67	1003.00	1303.56
265.67	1255.00	1304.92
265.67	1501.00	1306.29
265.67	2007.00	1308.73
265.67	2506.00	1311.28
265.67	3005.00	1313.79
265.67	4004.00	1318.59
265.67	5004.00	1323.31
265.67	6005.00	1328.01
265.67	8002.00	1338.69
265.67	10001.00	1349.81
265.67	12001.00	1358.7
265.67	14003.00	1366.48
265.67	16050.00	1375.48
265.67	18001.00	1384.77
265.67	20003.00	1394.13
265.67	23001.00	1407.08
265.67	27004.00	1425.32
265.67	31003.00	1439.78
265.67	34997.00	1455.17
265.67	39999.00	1476.05
265.67	45002.00	1494.61
265.67	49999.00	1511.6
265.67	55001.00	1528.77
265.67	60002.00	1548.05
265.67	65000.00	1564.17
265.67	18001.00	1384.54
273.16	102.00	1264.48
273.16	504.00	1266.57
273.16	750.00	1267.96
273.16	1003.00	1269.39
273.16	1255.00	1270.74
273.16	1501.00	1272.23
273.16	2007.00	1275.12
273.16	2506.00	1277.93
273.16	3005.00	1281.1
273.16	4004.00	1287.23
273.16	5004.00	1291.97
273.16	6005.00	1296.6
273.16	8002.00	1306.58
273.16	10001.00	1316.19
273.16	12001.00	1325.58
273.16	14003.00	1335.9
273.16	16005.00	1346.87
273.16	18001.00	1355.99
273.16	20003.00	1363.63
273.16	23001.00	1376.52
273.16	27004.00	1394.61
273.16	31003.00	1412.24
273.16	34997.00	1428.86
273.16	39999.00	1446.67
273.16	45002.00	1467.44
273.16	49999.00	1485.84
273.16	55001.00	1504.31
273.16	60002.00	1520.08
273.16	65000.00	1538.71
273.16	3005.00	1281.19
273.16	4004.00	1286.78
273.16	5004.00	1292.02
280.74	75.00	1233.63
280.74	504.00	1234.94
280.74	750.00	1236.39
280.74	1003.00	1237.85
280.74	1255.00	1239.22
280.74	1501.00	1240.59
280.74	2007.00	1243.75
280.74	2506.00	1247.03
280.74	3005.00	1249.76
280.74	4004.00	1255.13
280.74	5004.00	1259.87
280.74	6005.00	1264.8
280.74	8002.00	1275.79
280.74	10001.00	1286.82
280.74	12001.00	1296.79
280.74	14003.00	1306.71
280.74	16005.00	1316.23
280.74	18001.00	1325.46
280.74	20003.00	1335.09
280.74	23001.00	1350.8
280.74	27004.00	1366.99
280.74	31003.00	1384.26
280.74	34997.00	1401.32
280.74	39999.00	1423.56
280.74	45002.00	1441.37
280.74	49999.00	1461.28
280.74	55001.00	1480.44
280.74	60002.00	1498.97
280.74	65000.00	1514.56
280.74	75.00	1232.04
280.74	23001.00	1350.8
280.74	39999.00	1423.74
280.74	45002.00	1441.37
280.74	60002.00	1498.91
280.74	65000.00	1514.63
288.23	109.00	1199.01
288.23	504.00	1201.24
288.23	750.00	1202.57
288.23	1003.00	1204.2
288.23	1255.00	1205.54
288.23	1501.00	1206.97
288.23	2007.00	1209.92
288.23	2506.00	1212.8
288.23	3005.00	1215.61
288.23	4004.00	1221.35
288.23	5004.00	1227.14
288.23	6005.00	1232.71
288.23	8002.00	1244.39
288.23	10001.00	1255.4
288.23	12001.00	1265.22
288.23	14003.00	1275.63
288.23	16005.00	1286.61
288.23	18001.00	1296.18
288.23	20003.00	1305.89
288.23	23001.00	1319.61
288.23	27004.00	1339.05
288.23	31003.00	1357.37
288.23	34997.00	1373.83
288.23	39999.00	1395.08
288.23	45002.00	1416.1
288.23	49999.00	1435.37
288.23	55001.00	1453.97
288.23	60002.00	1473.72
288.23	65000.00	1492.08
298.23	109.00	1153.69
298.23	504.00	1156.23
298.23	750.00	1157.82
298.23	1003.00	1159.5
298.23	1255.00	1161.14
298.23	1501.00	1162.71
298.23	2007.00	1165.65
298.23	2506.00	1168.6
298.23	3005.00	1171.49
298.23	4004.00	1177.4
298.23	5004.00	1182.9
298.23	6005.00	1189.6
298.23	8002.00	1201.45
298.23	10001.00	1212.8
298.23	12001.00	1223.83
298.23	14003.00	1234.83
298.23	16005.00	1246.18
298.23	18001.00	1256.46
298.23	20003.00	1265.92
298.23	23001.00	1281.93
298.23	27004.00	1301.17
298.23	31003.00	1319.28
298.23	34997.00	1337.9
298.23	39999.00	1359.25
298.23	45002.00	1380.44
298.23	49999.00	1400.61
298.23	55001.00	1421.32
298.23	60002.00	1439.68
298.23	65000.00	1458.59
308.22	109.00	1107.74
308.22	504.00	1110.52
308.22	750.00	1112.35
308.22	1003.00	1114.01
308.22	1255.00	1115.75
308.22	1501.00	1117.34
308.22	2007.00	1120.69
308.22	2506.00	1123.91
308.22	3005.00	1127.11
308.22	4004.00	1133.79
308.22	5004.00	1140.56
308.22	6005.00	1146.98
308.22	8002.00	1159.51
308.22	10001.00	1171.13
308.22	12001.00	1182.37
308.22	14003.00	1194.75
308.22	16005.00	1205.76
308.22	18001.00	1216.57
308.22	20003.00	1227.49
308.22	23001.00	1244.05
308.22	27004.00	1263.44
308.22	31003.00	1283.97
308.22	34997.00	1302.46
308.22	39999.00	1324.45
308.22	45002.00	1347.09
308.22	49999.00	1367.79
308.22	55001.00	1388.31
308.22	60002.00	1408.07
308.22	65000.00	1427.73
318.22	109.00	1062.32
318.22	504.00	1065.38
318.22	750.00	1067.34
318.22	1003.00	1069.21
318.22	1255.00	1071.11
318.22	1501.00	1072.72
318.22	2007.00	1076.32
318.22	2506.00	1079.71
318.22	3005.00	1083.5
318.22	4004.00	1090.38
318.22	5004.00	1096.85
318.22	6005.00	1103.61
318.22	8002.00	1116.61
318.22	10001.00	1129.13
318.22	12001.00	1142.47
318.22	14003.00	1154.62
318.22	16005.00	1166.43
318.22	18001.00	1177.61
318.22	20003.00	1189.14
318.22	23001.00	1205.63
318.22	27004.00	1226.77
318.22	31003.00	1247.41
318.22	34997.00	1266.28
318.22	39999.00	1290.76
318.22	45002.00	1313.78
318.22	49999.00	1334.83
318.22	55001.00	1356.46
318.22	60002.00	1376.77
318.22	65000.00	1395.43
328.22	129.00	1018.3
328.22	504.00	1021.14
328.22	750.00	1023.1
328.22	1003.00	1024.91
328.22	1255.00	1026.82
328.22	1501.00	1028.6
328.22	2007.00	1032.33
328.22	2506.00	1036.21
328.22	3005.00	1040.05
328.22	4004.00	1047.07
328.22	5004.00	1053.76
328.22	6005.00	1060.7
328.22	8002.00	1074.73
328.22	10001.00	1088.42
328.22	12001.00	1101.14
328.22	14003.00	1113.97
328.22	16005.00	1126.49
328.22	18001.00	1138.92
328.22	20003.00	1151.08
328.22	23001.00	1168.1
328.22	27004.00	1190.45
328.22	31003.00	1211.66
328.22	34997.00	1231.66
328.22	39999.00	1256.67
328.22	45002.00	1280.63
328.22	49999.00	1303.34
328.22	55001.00	1324.67
328.22	60002.00	1345.81
328.22	65000.00	1365.57
338.22	170.00	972.8
338.22	504.00	976.32
338.22	750.00	978.88
338.22	1003.00	981.05
338.22	1255.00	982.97
338.22	1501.00	984.75
338.22	2007.00	988.42
338.22	2506.00	992.07
338.22	3005.00	996.0
338.22	4004.00	1004.26
338.22	5004.00	1011.63
338.22	6005.00	1019.16
338.22	8002.00	1033.34
338.22	10001.00	1047.72
338.22	12001.00	1061.19
338.22	14003.00	1074.71
338.22	16005.00	1088.09
338.22	18001.00	1100.33
338.22	20003.00	1112.58
338.22	23001.00	1131.02
338.22	27004.00	1154.76
338.22	31003.00	1176.19
338.22	34997.00	1197.57
338.22	39999.00	1223.29
338.22	45002.00	1248.14
338.22	49999.00	1271.19
338.22	55001.00	1293.31
338.22	60002.00	1315.39
338.22	65000.00	1336.38
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Speed of sound, m/s - Liquid
248.15	100.00	1390.16
248.15	10000.00	1435.51
248.15	20000.00	1478.36
248.15	30000.00	1518.03
248.15	40000.00	1550.78
248.15	50000.00	1590.88
248.15	60000.00	1625.12
248.15	70000.00	1657.38
248.15	80000.00	1688.07
248.15	90000.00	1717.48
248.15	100000.00	1745.43
253.15	100.00	1367.16
253.15	10000.00	1413.84
253.15	20000.00	1457.41
253.15	30000.00	1497.98
253.15	40000.00	1536.44
253.15	50000.00	1572.26
253.15	60000.00	1606.9
253.15	70000.00	1639.52
253.15	80000.00	1670.88
253.15	90000.00	1700.93
253.15	100000.00	1729.65
258.15	100.00	1344.2
258.15	10000.00	1391.98
258.15	20000.00	1436.58
258.15	30000.00	1478.11
258.15	40000.00	1517.33
258.15	50000.00	1553.89
258.15	60000.00	1588.88
258.15	70000.00	1621.91
258.15	80000.00	1653.89
258.15	90000.00	1684.43
258.15	100000.00	1713.62
263.15	100.00	1320.92
263.15	10000.00	1370.35
263.15	20000.00	1415.99
263.15	30000.00	1458.25
263.15	40000.00	1498.44
263.15	50000.00	1535.81
263.15	60000.00	1570.98
263.15	70000.00	1604.54
263.15	80000.00	1637.11
263.15	90000.00	1668.1
263.15	100000.00	1697.74
268.15	100.00	1298.67
268.15	10000.00	1349.08
268.15	20000.00	1395.62
268.15	30000.00	1438.54
268.15	40000.00	1479.77
268.15	50000.00	1517.83
268.15	60000.00	1553.2
268.15	70000.00	1587.43
268.15	80000.00	1620.54
268.15	90000.00	1651.96
268.15	100000.00	1682.01
273.15	100.00	1275.4
273.15	10000.00	1327.81
273.15	20000.00	1375.45
273.15	30000.00	1418.96
273.15	40000.00	1461.31
273.15	50000.00	1499.98
273.15	60000.00	1535.77
273.15	70000.00	1570.58
273.15	80000.00	1604.15
273.15	90000.00	1636.02
273.15	100000.00	1666.45
278.15	100.00	1253.32
278.15	10000.00	1306.75
278.15	20000.00	1355.49
278.15	30000.00	1400.47
278.15	40000.00	1443.03
278.15	50000.00	1481.78
278.15	60000.00	1518.62
278.15	70000.00	1553.98
278.15	80000.00	1587.94
278.15	90000.00	1620.26
278.15	100000.00	1650.92
283.15	100.00	1231.06
283.15	10000.00	1285.85
283.15	20000.00	1335.74
283.15	30000.00	1381.4
283.15	40000.00	1424.94
283.15	50000.00	1464.43
283.15	60000.00	1502.23
283.15	70000.00	1537.63
283.15	80000.00	1571.96
283.15	90000.00	1604.68
283.15	100000.00	1635.63
288.15	100.00	1208.58
288.15	10000.00	1265.05
288.15	20000.00	1316.19
288.15	30000.00	1362.56
288.15	40000.00	1407.06
288.15	50000.00	1447.7
288.15	60000.00	1485.52
288.15	70000.00	1521.53
288.15	80000.00	1556.22
288.15	90000.00	1589.2
288.15	100000.00	1620.74
293.15	100.00	1186.09
293.15	10000.00	1244.14
293.15	20000.00	1296.86
293.15	30000.00	1344.06
293.15	40000.00	1389.16
293.15	50000.00	1430.7
293.15	60000.00	1469.0
293.15	70000.00	1505.7
293.15	80000.00	1540.77
293.15	90000.00	1574.27
293.15	100000.00	1605.01
298.15	100.00	1165.34
298.15	10000.00	1223.74
298.15	20000.00	1277.93
298.15	30000.00	1325.68
298.15	40000.00	1371.61
298.15	50000.00	1413.84
298.15	60000.00	1452.64
298.15	70000.00	1490.14
298.15	80000.00	1525.25
298.15	90000.00	1559.14
298.15	100000.00	1591.53
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 4731.33]	kPa	[240.93; 508.10]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.48340e+01
Coefficient B			-3.02945e+03
Coefficient C			-3.26710e+01
Temperature range, min.			240.93
Temperature range, max.			508.10
Pvap	1.33	kPa	240.93	Calculated Property
Pvap	8.18	kPa	270.62	Calculated Property
Pvap	33.60	kPa	300.30	Calculated Property
Pvap	104.03	kPa	329.99	Calculated Property
Pvap	262.34	kPa	359.67	Calculated Property
Pvap	567.19	kPa	389.36	Calculated Property
Pvap	1089.25	kPa	419.04	Calculated Property
Pvap	1905.84	kPa	448.73	Calculated Property
Pvap	3095.17	kPa	478.41	Calculated Property
Pvap	4731.33	kPa	508.10	Calculated Property
Pvap	[2.57e-03; 4695.88]	kPa	[178.45; 508.20]	KDB Vapor Pressure Data
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			6.69693e+01
Coefficient B			-5.78459e+03
Coefficient C			-7.85881e+00
Coefficient D			7.10496e-06
Temperature range, min.			178.45
Temperature range, max.			508.20
Pvap	2.57e-03	kPa	178.45	Calculated Property
Pvap	0.16	kPa	215.09	Calculated Property
Pvap	2.70	kPa	251.73	Calculated Property
Pvap	19.81	kPa	288.37	Calculated Property
Pvap	87.11	kPa	325.01	Calculated Property
Pvap	273.04	kPa	361.64	Calculated Property
Pvap	678.92	kPa	398.28	Calculated Property
Pvap	1435.57	kPa	434.92	Calculated Property
Pvap	2705.52	kPa	471.56	Calculated Property
Pvap	4695.88	kPa	508.20	Calculated Property

Similar Compounds

Find more compounds similar to Acetone.

Mixtures

• Toluene + Acetone
• Ethanol + Acetone
• Acetone + Pentane, 2,2,4-trimethyl-
• Ethanol + Acetone + Pentane, 2,2,4-trimethyl-
• Diethyl carbonate + Acetone
• Acetone + Methyl Alcohol
• Benzoic acid, 4-nitro- + Benzoic acid, 2-nitro- + Acetone
• Diisopropyl ether + Acetone
• Acetone + Cyclohexane
• Diisopropyl ether + Acetone + Cyclohexane
• Propane, 2-methoxy-2-methyl- + Acetone
• Propane, 2-methoxy-2-methyl- + Acetone + Cyclohexane
• Butanedioic acid, methylene- + Acetone
• Acetone + 2-Propanone, O-methyloxime
• Acetone + 1-Propanamine, N-propyl-
• 1-Butanamine, N-butyl- + Acetone
• Triethylamine + Acetone
• Acetone + D-malic acid
• Hexane, 1-bromo- + Acetone
• 1H-Imidazole, 1-methyl- + Acetone

Find more mixtures with Acetone.

Sources

• KDB Pure (Korean Thermophysical Properties Databank)
• KDB Vapor Pressure Data
• Cheméo Relay (1.0)
• Crippen Method
• Crippen Method
• Dortmund Data Bank Vapor-Liquid Equilibrium Data
• Study of Acoustic Parameters in Binary Mixture at Variable Frequencies
• Measurement and prediction of vapor-liquid equilibria of ternary systems containing ionic liquids
• Measurement and correlation of vapor liquid equilibria of binary systems containing the ionic liquids [EMIM][(CF3SO2)2N], [BMIM][(CF3SO2)2N], [MMIM][(CH3)2PO4] and oxygenated organic compounds respectively water
• Isobaric vapor liquid equilibria for mixtures of acetone, ethanol, and 2,2,4-trimethylpentane at 101.3 kPa
• A relative headspace method for Henry s constants of volatile organic compounds
• Vapor liquid equilibria for systems of diethyl carbonate and ketones and determination of group interaction parameters for the UNIFAC and ASOG methods
• Vapor liquid liquid equilibria of perfluorohexane +CO2 + methanol, +toluene, and +acetone at 313K
• Isobaric vapor liquid equilibria for acetone + methanol + lithium nitrate at 100 kPa
• Experimental isobaric vapour liquid liquid equilibrium data for the quaternary systems water (1) ethanol (2) acetone (3) n-butyl acetate (4) and water (1) ethanol (2) acetone (3) methyl ethyl ketone (4) and their partially miscible-constituent ternaries
• Liquid liquid equilibria of 1,3-dimethylimidazolium methyl sulfate with ketones, dialkyl carbonates and acetates
• Measurement of vapor.liquid equilibria (VLE) and excess enthalpies (HE) of binary systems with 1-alkyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide and prediction of these properties and A using modified UNIFAC (Dortmund)
• Solubility of sodium diclofenac in different solvents
• Solubilities of rutin in eight solvents at T = 283.15, 298.15, 313.15, 323.15, and 333.15K
• Measurements of the solubilties of m-phthalic acid in acetone, ethanol and acetic ether
• Solid liquid phase equilibrium and phase diagram for ternary o-nitrobenzoic acid p-nitrobenzoic acid acetone system at 283.15K and 313.15K
• Vapor liquid equilibria and interfacial tensions for the ternary system acetone + 2,2 -oxybis[propane] + cyclohexane and its constituent binary systems
• Phase equilibria and interfacial tensions in the systems methyl tert-butyl ether + acetone + cyclohexane, methyl tert-butyl ether + acetone and methyl tert-butyl ether + cyclohexane
• Measurement of solubility of erythromycin acetone solvate in aqueous acetone solution between 298K and 323K
• Solid liquid equilibria of the ternary system m-nitrobenzoic acid + p-nitrobenzoic acid + acetone
• Activity coefficients at infinite dilution measurements for organic solutes and water in the 1-hexyloxymethyl-3-methyl-imidazolium and 1,3-dihexyloxymethyl-imidazolium bis(trifluoromethylsulfonyl)-imide ionic liquids The cation influence
• Measurement and prediction of multicomponent diffusion coefficients in four ternary liquid systems
• Compact apparatus for rapid measurement of high-pressure phase equilibria of carbon dioxide expanded liquids
• Solubility of benzoic acid in acetone, 2-propanol, acetic acid and cyclohexane: Experimental measurement and thermodynamic modeling
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
• Solubility of alpha-form and beta-form of L-glutamic acid in different aqueous solvent mixtures
• Liquid densities of acetone and n-heptane and excess volumes of the binary system in a wide temperature and pressure range
• Measurement and correlation of solubility of benzamide in supercritical carbon dioxide with and without cosolvent
• Experimental determination and calculation of the critical curves for the binary systems of CO2 containing ketone, alkane, ester and alcohol, respectively
• Solubility of itaconic acid in different organic solvents: Experimental measurement and thermodynamic modeling
• Determination of the solubility, dissolution enthalpy and entropy of pyrene in different solvents
• Thermodynamics of the solubility of lomefloxacin in methanol, ethanol, 1-propanol, 2-propanol, acetone, and chloroform from 293.15 to 323.15 K
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid ethyl(2-hydroxyethyl)dimethyl-ammonium diethylphosphate using gas liquid chromatography
• Solid-liquid phase equilibrium of glyphosate in selected solvents
• Activity coefficients at infinite dilution of organic solutes in 1-octyl-3-methylimidazolium nitrate using gas-liquid chromatography
• Solubility of lansoprazole in different solvents
• Determination of the solubility, dissolution enthalpy and entropy of suberic acid in different solvents
• Thermodynamic analysis and correlation of solubility of candesartan cilexetil in aqueous solvent mixtures
• Solid liquid equilibrium of 1-hydroxyethane-1,1-diphosphonic acid in different solvents
• Influence of sulfate-based anion ionic liquids on the separation factor of the binary azeotropic system acetone + methanol
• Isobaric vapor-liquid equilibria of the binary system acetone + acetone oxime methyl ether at 101.3 kPa
• Thermodynamics of ketone + amine mixtures. Part IX. Excess molar enthalpies at 298.15K for dipropylamine, or dibutylamine + 2-alkanone systems and modeling of linear or aromatic amine + 2-alkanone mixtures in terms of DISQUAC and ERAS
• Solubility of propanoic acid 3-(hydroxyphenylphosphinyl)-sodium salts in different solvent
• Thermodynamics of solubility of thiomalic acid in different organicsolvents from 278.15 K to 333.15 K
• Correlation of solubility of pioglitazone hydrochloride in different binary solvents
• Measurement and correlation solubility and mixing properties of dimethyl succinylsuccinate in pure and mixture organic solvents from (278.15 to 333.15) K
• Thermodynamics of ketone + amine mixtures. Part X. Excess molarenthalpies at 298.15 K for N,N,N-triethylamine + 2-alkanone systems.Characterization of tertiary amine + 2-alkanone, and ofamino-ketone + n-alkane mixtures in terms of DISQUAC
• A novel dynamic recirculating apparatus for vapour-liquid equilibrium measurements at moderate pressures and temperatures
• Measurement and calculation of solid-liquid phase equilibrium for ternary 4-chlorophthalic anhydride + 3-chlorophthalic anhydride + acetone system
• Solubility of 1, 3, 2-dioxaphosphorinane-5,5-dimethyl -2- (2,4,6-tribromophenoxy)-2-oxide in selected solvents
• A Raman spectroscopic method for the determination of high pressure vapour liquid equilibria
• Measurement and correlation solubility and mixing properties of L-malic acid in pure and mixture organic solvents
• Measurements of activity coefficients at infinite dilution in vegetable oils and capric acid using the dilutor technique
• The solubility of mercaptosuccinic acid in water + (methanol, ethanol, acetone) mixtures from (278.15 to 333.15 K)
• Determination and correlation of cefoperazone solubility in different pure solvents and binary mixture
• Vapor-liquid equilibrium in the production of the ionic liquid, 1-hexyl-3-methylimidazolium bromide ([HMIm][Br]), in acetone
• Solid-liquid equilibrium of dicyandiamide in different solvents
• Measurement and correlation of the solubility of maleic anhydride in different organic solvents
• Thermodynamics of fenofibrate and solubility in pure organic solvents
• Measurement and correlation of the solubilities of tetra(5,5-dimethyl-1,3-dioxaphosphorinanyl-2-oxy) neopentane in different pure solvents
• The determination and correlation of the solubility of naproxen in acetone and water mixtures
• Determination and correlation of solubility and solution thermodynamics of valnemulin hydrogen tartrate in different pure solvents
• High-pressure solubility of naproxen, nicotinamide and their mixture in acetone with supercritical CO2 as an anti-solvent
• Thermostabilities and solubilities of flame retardant bisphenol S-bis (5,5-dimethyl-1,3-dioxaphosphorinanyl-2-oxy phosphate ester) as a function of temperature
• Solubility and polymorphic forms of antibiotic lasalocid sodium in different organic solvents
• Thermodynamics of risperidone and solubility in pure organic solvents
• Solid-liquid equilibrium and thermodynamic of 2,5-thiophenedicarboxylic acid in different organic solvents
• 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
• Separation of acetone and methanol azeotropic system using ionic liquid as entrainer
• Solubility and thermodynamic functions of cefazolin acid in pure and mixed solvents at (278.15 308.15) K
• Solubilities of phosphoric acid, P,P0-1,4-phenylene P,P,P0,P0-tetraphenyl ester in the organic solvents
• Correlation of solubility and calculation of thermodynamic properties of guanidine nitrate in different solvents
• Thermodynamic analysis and correlation of solubility of Cefaclor in different solvents from 278.15 to 313.15 K
• Solubility of methylphosphonic acid in selected organic solvents
• Separation of pyridine from heptane with tricyanomethanide-based ionic liquids
• Solid-liquid equilibrium of diphenyl anilinophosphonate in the different organic solvents
• Measurement and correlation of solubility and dissolution properties of flunixin meglumine in pure and binary solvents
• Thermodynamic models for determination of the solid-liquid equilibrium of oxytocin in (acetonitrile + acetone) binary solvent mixtures
• Activity coefficients at infinite dilution for different alcohols and ketones in [EMpy][ESO4]: Experimental data and modeling with PC-SAFT
• Measurement and correlation of ternary solid-liquid equilibrium of 2-methyl-1,4-naphthoquinone + phthalic anhydride + acetone system
• 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
• Solubility of D-phenylglycine methyl ester hydrochloride in water and in organic individual or mixed solvents: Experimental data and results of thermodynamic modeling
• Abraham model linear free energy relationships for describing the partitioning and solubility behavior of nonelectrolyte organic solutes dissolved in pyridine at 298.15 K
• Isothermal vapour-liquid equilibrium data for the binary systems 2-propanone + (2-butanol or propanoic acid)
• Coupled phase-reaction equilibrium for dihydromyrcene hydration system
• Equilibrium study and diversified models of drug Norfloxacin in eight pure organic and binary solvents at T = (278.15 to 328.15) K
• In situ measurement of liquid-liquid equilibria by medium field nuclear magnetic resonance
• Isobaric vapor-liquid equilibrium for ternary mixtures of acetone + methanol + ionic liquids at 101.3kPa
• High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
• Thermodynamic equilibrium of hydrocortisone form I in different solvent systems
• Isobaric vapor-liquid equilibrium for acetone + methanol system containing different ionic liquids at 101.3 kPa
• Gas solubilities of carbon dioxide in methanol, acetone, mixtures of methanol and water, and mixtures of methanol and acetone
• Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
• Solubility and mixing thermodynamic properties of (2,4,6-trimethylbenzoyl) diphenylphosphine oxide in pure and binary solvents
• Measurements of activity coefficient at infinite dilution for organic solutes in tetramethylammonium chloride + ethylene glycol deep eutectic solvent using gas-liquid chromatography
• 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
• Tetramethylammonium chloride + glycerol deep eutectic solvent as separation agent for organic liquid mixtures: Assessment from experimental limiting activity coefficients
• High-pressure phase equilibrium data for carbon dioxide p dichloromethane p acetone and carbon dioxide p dichloromethane p acetone p N-acetylcysteine (NAC)
• Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-butyl-1-methylpyrrolidinium dicyanamide
• Solubility determination and correlation of cyromazine in sixteen pure solvents and mixing properties of solutions
• New ionic liquid [P4,4,4,4][NTf2] in bio-butanol extraction on investigation of limiting activity coefficients
• The behavior of mercury in water, alcohols, monoethylene glycol and triethylene glycol II. Elemental mercury solubility in alcohols, ethers and acetone; gas plant mercury distribution; and speciation in monoethylene glycol solution
• Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
• Densities, viscosities, and refractive indices of binary and ternary mixtures of methanol, acetone, and chloroform at temperatures from (298.15-318.15) K and ambient pressure
• Measurements of activity coefficients at infinite dilution for organic solutes in two quaternary ammonium-based ionic liquids [DDA][ClO4] and [DDA][BF4]
• 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
• Solubility measurements and thermodynamic modeling of pyrazinamide in five different solvent-antisolvent mixtures
• Solubility and density of the disodium salt hemiheptahydrate of ceftriaxone in (acetone + water) at T=(298.15,308.15, and 318.15) K
• A novel non-intrusive microcell for sound-speed measurements in liquids. Speed of sound and thermodynamic properties of 2-propanone at pressures up to 160 MPa
• A thermodynamic study of the ketoreductase-catalyzed reduction of 2-alkanones in non-aqueous solvents
• Thermodynamics of binary mixtures of N-methyl-2-pyrrolidinone and ketone. Experimental results and modelling of the solid-liquid equilibrium and vapou-liquid equilibrium. The Modified UNIFAC (Do) model characterization
• Solubility of paroxetine hydrochloride hemi-hydrate in (water + acetone)
• Systems with ionic liquids: Measurement of VLE and c1 data and prediction of their thermodynamic behavior using original UNIFAC, mod. UNIFAC(Do) and COSMO-RS(Ol)
• Properties of ionic liquid HMIMPF6 with carbonates, ketones and alkyl acetates
• Physical properties of the binary systems methylcyclopentane with ketones (acetone, butanone and 2-pentanone) at T = (293.15, 298.15, and 303.15) K. New UNIFAC-VISCO interaction parameters
• (Vapour + liquid) equilibria for (2-ethoxypropene + acetone) and (2-ethoxypropene + butanone)
• Excess molar enthalpies and volumes of binary mixtures of nonafluorobutylmethylether with ketones at T = 298.15 K
• Density and speed of sound of lithium bromide with organic solvents: Measurement and correlation
• 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
• Thermodynamic properties of acetone calculated from accurate experimental speed of sound measurements at low temperatures and high pressures
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 4-methyl-N-butyl-pyridinium bis(trifluoromethylsulfonyl)-imide
• Activity coefficients at infinite dilution for solutes in the trioctylmethylammonium bis(trifluoromethylsulfonyl)imide ionic liquid using gas liquid chromatography
• Excess parameter studies on the binary mixtures of toluene with ketones at different temperatures
• 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.
• (Ternary liquid + liquid) equilibria for (water + acetone + alpha-pinene, or beta-pinene, or limonene) mixtures
• 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
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid trihexyl(tetradecyl)phosphonium tetrafluoroborate using gas liquid chromatography at T = (313.15, 333.15, 353.15, and 373.15) K
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-butyl-3-methylimidazolium hexafluoroantimonate using gas liquid chromatography at T = (313.15, 323.15, and 333.15) K
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid, methyl(trioctyl)ammonium thiosalicylate, [N1888][TS] by gas liquid chromatography at T = (303.15, 313.15, and 323.15) K
• Apparent molar volumes and compressibilities of tetrabutyl-ammonium bromide in organic solvents
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(3-hydroxypropyl)pyridinium bis(trifluoromethylsulfonyl)-amide
• Thermodynamics and activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tetracyanoborate
• Interactions of volatile organic compounds with the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
• Excess properties of binary mixtures containing 1-hexyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide ionic liquid and polar organic compounds
• Solubility of diosgenin in different solvents
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-hexyl-3-methylimidazolium tetracyanoborate
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid trihexyltetradecylphosphonium hexafluorophosphate using gas liquid chromatography at T = (313.15, 333.15, 353.15, and 363.15) K
• 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
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpyrrolidinium bis(trifluoromethylsulfonyl)-amide
• Phase diagrams of acetonitrile or (acetone + water + EPPS) buffer phase separation systems at 298.15 K and quantum chemical modeling
• Measurement and prediction of the solubilities of aromatic polyimide monomers in supercritical carbon dioxide with acetone
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium trifluorotris(perfluoroethyl)phosphate
• Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds: Saturated fatty acids
• 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
• Interactions of volatile organic compounds with the ionic liquids 1-butyl-1-methylpyrrolidinium tetracyanoborate and 1-butyl-1-methylpyrrolidinium bis(oxalato)borate
• Physicochemical properties and activity coefficients at infinite dilution for organic solutes and water in a novel bicyclic guanidinium superbase-derived protic ionic liquid
• Solubilities of evodiamine in twelve organic solvents from T = (283.2 to 323.2) K
• Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds Part II: C18 fatty acids
• Experimental and theoretical study on infinite dilution activity coefficients of various solutes in piperidinium ionic liquids
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpyrrolidinium trifluorotris(perfluoroethyl)phosphate
• Thermodynamic properties of binary mixtures of the ionic liquid [emim][BF4] with acetone and dimethylsulphoxide
• On the solubility of nicotinic acid and isonicotinic acid in water and organic solvents
• Measurements of activity coefficients at infinite dilution for organic solutes and water in N-hexylisoquinolinium thiocyanate, [HiQuin][SCN] using GLC
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-hydroxyethyl)- 3-methylimidazolium trifluorotris(perfluoroethyl)phosphate
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid trihexyltetradecylphosphonium bis(trifluoromethylsulfonyl)imide using gas-liquid chromatography at T = (313.15, 333.15, 353.15 and 373.15) K
• Infinite dilution activity coefficients of volatile organic compounds in two ionic liquids composed of the tris(pentafluoroethyl) trifluorophosphate ([FAP]) anion and a functionalized cation
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tricyanomethanide
• Thermodynamics and activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylmorpholinium tricyanomethanide
• The study of activity coefficients at infinite dilution for organic solutes and water in 1-butyl-4-methylpyridinium dicyanamide, [B4MPy][DCA] using GLC
• Measurement and correlation of solubility of dodecanedioic acid in different pure solvents from T = (288.15 to 323.15) K
• Separation of sulfur compounds from alkanes with 1-alkylcyanopyridinium-based ionic liquids
• Measurement of activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium 2-(2-methoxyethoxy) ethylsulfate at T = (308.15, 313.15, 323.15 and 333.15) K using gas + liquid chromatography
• Activity coefficients at infinite dilution of organic solutes in 1-hexyl-3- methylimidazolium trifluoroacetate and influence of interfacial adsorption using gas liquid chromatography
• Effect of the alkyl side chain of the 1-alkylpiperidinium-based ionic liquids on desulfurization of fuels
• Measurement, correlation and dissolution thermodynamics of biological active chalcone in organic solvents at different temperatures
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-butyl-3-methylimidazolium methyl sulfate
• Experimental measurement and modelling of solubility of inosine-5'-monophosphate disodium in pure and mixed solvents
• Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
• Extraction desulfurization process of fuels with ionic liquids
• An odd-even effect on solubility of dicarboxylic acids in organic solvents
• (Solid + liquid) phase equilibria of tetraphenyl piperazine-1,4-diyldiphosphonate in pure solvents
• VLE measurements using a static cell vapor phase manual sampling method accompanied with an empirical data consistency test
• 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
• Isothermal (vapor + liquid) equilibria for the binary mixtures of (propylene oxide + ethanol) and (propylene oxide + 1-propanol) at several temperatures
• (Liquid + liquid) equilibria for (water + 1-propanol or acetone + .beta.-citronellol) at different temperatures
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(3-hydroxypropyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
• Solubility of daidzin in different organic solvents and (ethyl alcohol + water) mixed solvents
• Activity coefficients at infinite dilution for organic solutes and water in 1-ethyl-1-methylpyrrolidinium lactate
• Measurement and correlation of the solubility of genistin in eleven organic solvents from T = (283.2 to 323.2) K
• Activity coefficients at infinite dilution, physicochemical and thermodynamic properties for organic solutes and water in the ionic liquid ethyl-dimethyl-(2-methoxyethyl)ammonium trifluorotris-(perfluoroethyl)phosphate
• Solubility of tridecanedioic acid in pure solvent systems: An experimental and computational study
• 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
• Solution thermodynamics of valnemulin hydrogen fumarate in different pure solvents
• 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
• Ionic liquid 1-hexyl-3-methylimidazolium hexafluorophosphate, an efficient solvent for extraction of acetone from aqueous solutions
• Determination and correlation of pyridoxine hydrochloride solubility in different binary mixtures at temperatures from (278.15 to 313.15) K
• Correlation and thermodynamic analysis of solubility of diphenhydramine hydrochloride in pure and binary solvents
• Solubility determination and correlation for 1,8-dinitronaphthalene in (acetone + methanol), (toluene + methanol) and (acetonitrile + methanol) mixed solvents
• Solubility modelling and thermodynamic dissolution functions of phthalimide in ten organic solvents
• Thermodynamic models for determination of the solubility of omeprazole in pure and mixture organic solvents from T = (278.15 to 333.15) K
• Solubility and solution thermodynamics of ethyl 5-amino-4-cyano-3-(2-ethoxy-2-oxoethyl)-2-thiophenecarboxylate in nine organic solvents at evaluated temperatures
• Determination and correlation of solubility and thermodynamic properties of L-methionine in binary solvents of water + (methanol, ethanol, acetone)
• Measurement and correlation of solubility and solution thermodynamics of 1,3-dimethylurea in different solvents from T = (288.15 to 328.15) K
• Solubility of 3-chloro-N-phenylphthalimide in ten organic solvents from T = (288.15 to 323.15) K: Determination and modelling
• A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
• Solubility measurement and thermodynamic functions of dehydroepiandrosterone acetate in different solvents at evaluated temperatures
• Thermodynamics of amide + ketone mixtures. 1. Volumetric, speed of sound and refractive index data for N,N-dimethylformamide + 2-alkanone systems at several temperatures
• 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
• Determination and modeling of the solubility of (limonin in methanol or acetone + water) binary solvent mixtures at T = 283.2 K to 318.2 K
• Thermodynamic models for determination of 3-chloro-N-phenylphthalimide solubility in binary solvent mixtures of (acetone, ethyl acetate or 1,4-dioxane + methanol)
• Solubility determination and thermodynamic modeling of 5-nitro-8- hydroxyquinoline in ten organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
• Solubility and solution thermodynamics of 2-methyl-6-nitroaniline in ten organic solvents at elevated temperatures
• 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
• Phase equilibria of the ternary systems of (water + diethyl carbonate) with acetone, or 2-butanone at four temperatures
• 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
• 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
• Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-hexyl-2,3-dimethylimidazolium bis(trifluoromethylsulfonyl)imide
• Solubility determination and thermodynamic modeling of 3-methyl-4- nitrobenzoic acid in twelve organic solvents from T = (283.15-318.15) K and mixing properties of solutions
• 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
• Solid-liquid phase equilibrium and mixing properties of 2-Cyano-4'-methylbiphenyl in pure solvents
• Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
• Solubility measurement and correlation of 4-nitrophthalimide in (methanol, ethanol, or acetone) + N,N-dimethylformamide mixed solvents at temperatures from 273.15 K to 323.15 K
• 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 determination and thermodynamic modelling of allisartan isoproxil in different binary solvent mixtures from T = (278.15 to 313.15) K and mixing properties of solutions
• Solubility measurement and modelling of ethyl 5-amino-4-cyano-3-(2-ethoxy-2-oxoethyl)-2-thiophenecarboxylate in four groups mixed solvents
• Separation of ethylbenzene/styrene systems using ionic liquids in ternary LLE
• 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
• Solubility determination and thermodynamic modelling of 3-amino-1,2,4-triazole in ten organic solvents from T = 283.15 K to T = 318.15 K and mixing properties of solutions
• Solubility measurement, model evaluation and thermodynamic analysis of rivaroxaban polymorphs in organic solvents
• Solubility determination and thermodynamic modeling of paclobutrazol in nine organic solvents from T = (278.15 to 318.15) K and mixing properties of solutions
• Solubility of L-histidine in different aqueous binary solvent mixtures from 283.15 K to 318.15 K with experimental measurement and thermodynamic modelling
• Determination and modeling of binary and ternary solid-liquid phase equilibrium for the systems formed by 3,5-dinitrobenzoic acid, m-nitrobenzoic acid and acetone
• Thermodynamic modelling for solubility of 5-chloro-1-methyl-4-nitroimidazole in eleven organic solvents from T = (283.15 to 318.15) K
• Understanding the enhanced solubility of 1,3-benzenedicarboxylic acid in polar binary solvents of (acetone + water) at various temperatures
• Thermodynamic properties of L-Theanine in different solvents
• Thermodynamic study of solubility for 2-amino-4-chloro-6-methoxypyrimidine in twelve organic solvents at temperatures from 273.15 K to 323.15 K
• Determination and correlation of Avermectin B1a solubility in different binary solvent mixtures at temperatures from (283.15 to 313.15) K
• Solid-liquid phase equilibrium and dissolution properties of ethyl vanillin in pure solvents
• Solubility and solution thermodynamics of 2-methyl-4-nitroaniline in eleven organic solvents at elevated temperatures
• Solubility measurement and thermodynamic functions of 3-nitrobenzaldehyde in different solvents at elevated temperatures
• Determination and correlation of solubility of 11alpha,17alpha-dihydroxy-4-pregnene-3,20-dione in different solvents
• Solubility determination and modelling of 4-nitro-1,2-phenylenediamine in eleven organic solvents from T = (283.15 to 318.15) K and thermodynamic properties of solutions
• Solubility determination and thermodynamic modelling for 2-amino-4-chlorobenzoic acid in eleven organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
• Solubility determination and modelling for phthalimide in mixed solvents of (acetone, ethyl acetate or acetonitrile + methanol) from (278.15 to 313.15) K
• Solubility determination and thermodynamic functions of 2-chlorophenothiazine in nine organic solvents from T = 283.15 K to T = 318.15 K and mixing properties of solutions
• Solubility and thermodynamic functions of tebuconazole in nine organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
• Thermodynamic models for determination of solid liquid equilibrium of the 6-benzyladenine in pure and binary organic solvents
• Solubility of 2-isopropylimidazole in nine pure organic solvents and liquid mixture of (methanol + ethyl acetate) from T = (278.15 to 313.15) K: Experimental measurement and thermodynamic modelling
• Thermodynamic equilibrium of hydroxyacetic acid in pure and binary solvent systems
• 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
• Ternary and binary LLE measurements for solvent (2-methyltetrahydrofuran and cyclopentyl methyl ether) + furfural + water between 298 and 343 K
• Thermodynamic functions for solubility of 3-nitro-o-toluic acid in nine organic solvents from T = (283.15 to 318.15) K and apparent thermodynamic properties of solutions
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
• Thermodynamic models for determination of the solid-liquid equilibrium of istradefylline in ethyl acetate plus (isopropanol, tetrahydrofuran, acetone) binary solvent mixtures
• Thermodynamic study of solubility for pyrazinamide in ten solvents from T = (283.15 to 323.15) K
• Solubility modelling and dissolution properties of 5-phenyltetrazole in thirteen mono-solvents and liquid mixtures of (methanol + ethyl acetate) at elevated temperatures
• Thermophysical approach to understand the nature of molecular interactions and structural factor between methyl isobutyl ketone and organic solvents mixtures
• Thermodynamics and activity coefficients at infinite dilution for organic compounds and water in the ionic liquid 1-butyl-3-methylimidazolium perchlorate
• Separation of water/butan-1-ol based on activity coefficients at infinite dilution in 1,3-didecyl-2-methylimidazolium dicyanamide ionic liquid
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on gamma infinity data measurements
• Separation of binary mixtures based on gamma infinity data using [OMMIM][NTf2] ionic liquid and modelling of thermodynamic functions
• Quaternary and ternary LLE measurements for solvent (2-methyltetrahydrofuran and cyclopentyl methyl ether) + furfural + acetic acid + water between 298 and 343 K
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid trihexyl-tetradecyl-phosphonium tricyanomethanide
• Thermodynamic study of molecular interaction-selectivity in separation processes based on limiting activity coefficients
• Isobaric vapour-liquid equilibrium measurements and extractive distillation process for the azeotrope of (N,N-dimethylisopropylamine + acetone)
• Abraham model correlations for describing the thermodynamic properties of solute transfer into pentyl acetate based on headspace chromatographic and solubility measurements
• Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in ionic liquid [HMMIM][BF4]
• The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
• Thermodynamics and activity coefficients at infinite dilution for organic compounds in the ionic liquid 1-hexyl-3-methylimidazolium chloride
• Separation of binary mixtures based on gamma infinity data using [OMMIM][BF4] ionic liquid and modelling of thermodynamic functions
• Solubility of dibenzothiophene in nine organic solvents: Experimental measurement and thermodynamic modelling
• Determination of the thermodynamic parameters of ionic liquid 1-propyl-3-methylimidazolium bromide by gas-liquid chromatography
• Ternary phase diagram of phenanthrene and carbazole in different solvents and its application in the separation of them
• The dissolution behavior and apparent thermodynamic analysis of temozolomide in pure and mixed solvents
• Solubility and thermodynamic properties of dirithromycin form A and form B in pure solvents and binary solvent mixture
• Research on the application of 7-chloro-quinaldine adducts in 7-chloro-quinaldine separation process
• Determination and correlation of solubility and solution thermodynamics of saccharin in different pure solvents
• Cosolvent effect on solubility of aripiprazole in mixed solvents and apparent thermodynamic analysis of dissolution process
• Separation of (water/butan-1-ol) binary systems based on activity coefficients at infinite dilution with phosphonium ionic liquid
• The dissolution behaviour and apparent thermodynamic analysis of diprophylline in pure and mixed solvents
• Co-solvence phenomenon and thermodynamic properties of edaravone in pure and mixed solvents
• Thermochemistry of 1-bromoadamantane in binary mixtures of water aprotic solvent
• Physical properties and their corresponding changes of mixing for the ternary mixture acetone + n-hexane +water at 298.15K
• Volumetric studies and thermodynamics of viscous flow of hydroxamic acids in acetone +water solvent at temperatures 303.15 and 313.15K
• Solubilities of succinimide in different pure solvents and binary methanol+ethyl acetate solvent mixtures
• Measurement and correlation of the solubility of maleic acid in acetone-ethyl acetate mixtures
• Determination of the solubility, dissolution enthalpy and entropy of 3-pentadecylphenyl acrylate in different organic solvents
• Solubility, dissolution enthalpy and entropy of L-Glutamine in mixed solvents of ethanol+water and acetone+water
• Measurement and correlation of phase diagram data for acetone andsulfate aqueous two-phase systems at different temperatures
• Isobaric specific heat capacities of emulsified kerosene at high temperature and pressure
• Experimental solubility and thermodynamic aspects of methylene blue in different solvents
• Solubilities of Phosphoramidic Acid, N-(phenylmethyl)-, Diphenyl Ester in Selected Solvents
• Solubility of 3,7-Dinitro-1,3,5,7-tetraazabicyclo [3.3.1] Nonane in Ethanenitrile, Methanol, 1,1-Dichloroethane, Dimethyl Sulfoxide, Acetone, and Mixed Solvents
• Dissociation Constants and Solubilities of Dalbergin and Nordalbergin in Different Solvents
• 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
• Solubility of Amorphous Clopidogrel Hydrogen Sulfate in Different Pure Solvents
• Lamotrigine Solubility in Some Nonaqueous Solvent Mixtures at 298.2 K
• Investigation of Surface and Solubility Properties of N-Vinylimidazolium Tetrahalogenidoferrate(III) Magnetic Ionic Liquids Using Density Functional Theory
• 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 Solubility of Cefathiamidine in Water + (Acetone, Ethanol, or 2-Propanol) from (278.15 to 308.15) K
• 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
• Ternary and Binary LLE Measurements for Solvent (4- Methyl-2-pentanone and 2-Methyl-2-butanol) + Furfural + Water between 298 and 401 K
• Solubility Determination and Modeling of Sodium Mononitrobenzenesulphonate in Different Solvents at Temperatures Ranging from (283.15 to 323.15) K
• Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
• Solubility Modeling of 4-(Methylsulfonyl)benzaldehyde in Nine Organic Solvents at Elevated Temperatures
• Determination and Correlation of Solubilities for Succinic Acid in the Adipic Acid + Glutaric Acid + Acetone Mixture and Adipic Acid in the Succinic Acid + Glutaric Acid + Acetone Mixture
• Quaternary, Ternary, and Binary LLE Measurements for 2-Methoxy-2-methylpropane + Furfural + Acetic Acid + Water at Temperatures between 298 and 307 K
• Quaternary, Ternary and Binary LLE Measurements for 2-Methoxy-2-methylbutane + Furfural + Acetic Acid + Water at Temperatures between 298 and 341 K
• Isobaric Vapor Liquid Equilibrium for Nine Binary Systems of Cracking C5 Fraction at 250 kPa
• Solubility Measurement and Thermodynamic Modeling of 4-Nitrophthalimide in Twelve Pure Solvents at Elevated Temperatures Ranging from (273.15 to 323.15) K
• Solubility of Fenofibrate in Different Binary Solvents: Experimental Data and Results of Thermodynamic Modeling
• Solubility of 3,7,9,11-Tetraoxo-2,4,6,8,10-pentaaza[3.3.3] Propellane (TOPAP) in Different Pure Solvents at Temperatures between 273.15 and 318.15 K
• Measurement and Correlation of the Solubility of p-Coumaric Acid in Nine Pure and Water + Ethanol Mixed Solvents at Temperatures from 293.15 to 333.15 K
• Solubility Determination and Modeling for 4,4'-Dihydroxydiphenyl Sulfone in Mixed Solvents of (Acetone, Ethyl Acetate, or Acetonitrile) + Methanol and Acetone + Ethanol from (278.15 to 313.15) K
• Measurement of Solubility of Thiamine Hydrochloride Hemihydrate in Three Binary Solvents and Mixing Properties of Solutions
• Solubility and Thermodynamic Behavior of Veramoss in Different Pure Solvents and {Ethanol + Water} Mixtures from T = 283.15 to 333.15 K
• Solubility Measurement and Correlation for e-2,4,6,8,10,12-Hexanitro-2,4,6,8,10,12-hexaazaisowurtzitane in Five Organic Solvents at Temperatures between 283.15 and 333.15 K and Different Chloralkane + Ethyl Acetate Binary Solvents at Temperatures between 283.15 and 323.15 K
• Vapor Liquid Equilibrium Data for Binary Mixtures of Acetic Acid + Anisole, Acetone + Anisole, and Isopropanol + Anisole at Pressure 96.15 kPa
• Measurement and Correlation of Solubility of Loratadine in Different Pure Solvents and Binary Mixtures
• Solubility Measurement and Correlation of Two Erlotinib Hydrochloride Polymorphs in Alcohols and Ketones from 273.15 to 323.15 K
• Solubility Measurement and the Correlation of 1-Naphthaleneacetic Acid in Pure and Methanol + Water Binary Solvents from T = (278.25 to 323.55) 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
• Determination and Correlation of Ethyl Vanillin Solubility in Different Binary Solvents at Temperatures from 273.15 to 313.15 K
• Measurement and Correlation of Solubility of Theobromine, Theophylline, and Caffeine in Water and Organic Solvents at Various Temperatures
• Pressurized-Synthetic Methodology for Solubility Determination at Elevated Temperatures with Application to Paracetamol in Pure Solvents
• Solid Liquid Phase Equilibrium of N,N'-Piperazinebis(neopentylglycol)phosphoramidate in Selected Solvents from T = (293.15 to 333.15) K
• Solubility of Benzoin in Six Monosolvents and in Some Binary Solvent Mixtures at Various Temperatures
• Determination of Infinite Dilution Activity Coefficients of Several Organic Solutes in N-Butylpyridinium Nitrate/N-Octylpyridinium Nitrate by Blend Inverse Gas Chromatography
• Experimental and Modeling Studies on the Solubility of 2-Chloro-N-(4-methylphenyl)propanamide (S1) in Binary Ethyl Acetate + Hexane, Toluene + Hexane, Acetone + Hexane, and Butanone + Hexane Solvent Mixtures Using Polythermal Method
• Measurement and Correlation of Solubility of Two Isomers of Cyanopyridine in Eight Pure Solvents from 268.15 K to 318.15 K
• Thermodynamic Functions for Solubility of 1-Hydroxybenzotriazole in Sixteen Solvents at Temperatures from (278.15 to 313.15) K and Mixing Property of Mixtures
• Determination and Correlation of Solubility of Quetiapine Fumarate in Nine Pure Solvents and Two Aqueous Binary Solvents
• Solubility in Different Solvents, Crystal Polymorph and Morphology, and Optimization of Crystallization Process of AIBN
• Solubility Modeling and Mixing Thermodynamics of Thiamphenicol in Water and Twelve Neat Organic Solvents from T = (278.15 to 318.15) K
• Synthesis and Solubility of 5,5-Dimethyl-2-(phenyl(phenylamino)methyl)-1,3,2-dioxaphosphinane 2-oxide in Selected Solvents between 278.15 K and 347.15 K
• Isothermal Vapor-Liquid Equilibria for Binary Mixtures of Methyl Nonafluorobutyl Ether + Acetone, Cyclopentyl Methyl Ether, Ethyl Acetate, n-Heptane, Methanol, and Toluene
• Thermodynamic Functions for the Solubility of 3-Nitrobenzonitrile in 12 Organic Solvents from T/K = (278.15 to 318.15)
• Solubility Measurement and Correlation of Fosfomycin Sodium in Six Organic Solvents and Different Binary Solvents at Temperatures between 283.15 and 323.15 K
• 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 Solubility of Resorcinol Bis(cyclic 2,2-dimethyl-1,3-propanediol phosphate) in Selected Solvents from T = 293.15 to 333.15 K
• Solubility Modeling and Mixing Properties for Benzoin in Different Monosolvents and Solvent Mixtures at the Temperature Range from 273.15 to 313.15 K
• Determination, Correlation, and Application of Sodium l-Ascorbate Solubility in Nine Pure Solvents and Two Binary Solvents at Temperatures from 278.15 to 323.15 K
• Solubility Measurement and Thermodynamic Modeling of N-(4-Methylphenyl-Z-3-chloro-2-(phenylthio)propenamide in 12 Pure Solvents at Temperatures Ranging from 278.15 to 318.15 K
• Solution Thermodynamics of Benzotriazole in Different Pure Solvents
• Solubility of Ionic Liquid [Bmim]Ac in Supercritical CO2 Containing Different Cosolvents
• Solubility of Sulfachloropyridazine in Pure and Binary Solvent Mixtures and Investigation of Intermolecular Interactions
• Aniracetam Solubility in Pure and Binary Solvents: Effect of Molecular Interaction and Analysis of Crystallized Products
• Solubility Measurement and Thermodynamic Modeling of Benzoic Acid in Monosolvents and Binary Mixtures
• Determination of Activity Coefficients at Infinite Dilution of Organic Solutes in the Ionic Liquid 1-(2-Hydroxyethyl)-3-methylimidazolium Nonafluoro-1-butanesulfonate Using Gas-Liquid Chromatography
• Solubility of 2-Chlorophenylacetic Acid in 12 Pure Solvents from T = (273.15/283.15 to 318.15) K: Determination and Modeling
• Solubility Measurement and Modeling of 1-(3-nitrophenyl)Ethanone and 1-(4-nitrophenyl)Ethenone in Nine Pure Organic Solvents from T = (278.15 to 318.15) K and Mixing Properties of Solutions
• 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)
• Solubility Measurement and Modeling of 2-Amino-4,6-dichoropyrimidine in Ten Pure Solvents and (Ethyl Acetate + Ethanol) Solvent Mixtures
• Solubility Determination and Correlation for Pyridoxal 5-Phosphate Monohydrate in Different Binary Solvents from 278.15 K to 318.15 K
• Experiment and Computation of Solubility and Dissolution Properties for Enalapril Maleate and Its Intermediate in Pure Solvents
• Determination and Correlation of the Solubility of l-Fucose in Four Binary Solvent Systems at the Temperature Range from 288.15 to 308.15 K
• Influence of Different Solvent Properties and Composition for the Solubility of Iopromide
• 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
• Isobaric Vapor-Liquid Equilibrium Data for the Acetone + Hexamethyl Disiloxane + Ethyl Acetate Ternary System at 101.3 kPa: Determination and Correlation
• Solubilities of Organic Semiconductors and Nonsteroidal Anti-inflammatory Drugs in Pure and Mixed Organic Solvents: Measurement and Modeling with Hansen Solubility Parameter
• Solubility Determination of Nicotinamide and Its Application for the Cocrystallization with Benzoic Acid
• Solubility Measurements at 296 and 310 K and Physicochemical Characterization of Abiraterone and Abiraterone Acetate
• Measurement and Correlation of Solubility of 3-Hydroxy-2-naphthoic Acid in Ten Pure and Binary Mixed Organic Solvents from T = (293.15 to 333.15 K)
• Activity Coefficients at Infinite Dilution of Various Solutes in Tetrapropylammonium Bromide + 1,6-Hexanediol Deep Eutectic Solvent
• Solubility of Diflufenican in Pure and Binary Solvent Systems
• Determination of Activity Coefficients at Infinite Dilution of Solutes in N,N'-Di(2-ethylhexyl)isobutyramide Using Inverse Gas-Liquid Chromatography
• Solubility Determination and Correlation of Glibenclamide in 11 Monosolvents and (Acetone + Acetonitrile) Binary Solvents from 283.15 K to 323.15 K
• Solubility Measurement and Thermodynamic Properties of Levetiracetam in Pure and Mixed Solvents
• Determination and Modeling of Solid-Liquid Equilibrium for Ternary Systems of Terephthaldialdehyde + 4-Hydroxybenzaldehyde + Ethyl Acetate/Acetone
• Solid-Liquid Equilibrium of Isomaltulose in Five Pure Solvents and Four Binary Solvents from (283.15 to 323.15) K
• Solubility Measurement and Correlation of Probenecid in 12 Pure Organic Solvents and Thermodynamic Properties of Mixing of Solutions
• Measurement and Correlation of the Solubility of Tetramethylpyrazine in Nine Monosolvents and Two Binary Solvent Systems
• Measurement and Correlation of Solubility of Gatifloxacin in 12 Pure Solvents from 273.15 K to 318.15 K
• Solubility Measurement and Thermodynamic Model Correlation and Evaluation of 2-Chloro-5-nitroaniline in 12 Pure Solvents
• Solubility Determination and Correlation of Warfarin Sodium 2-Propanol Solvate in Pure, Binary, and Ternary Solvent Mixtures
• Equilibrium Solubility of Biapenem in Different Neat and Binary Solvents: Experimental Determination and Model Correlation
• Measurement and Correlation of the Solubility of Mifepristone in Eight Pure and Water + Methanol Mixed Solvents at Temperatures from 273.15 to 318.15 K
• Effect of Solvent Properties and Composition on the Solubility of Ganciclovir Form I
• 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
• Liquid Liquid Equilibrium Data for the Separation of Acetone from n-Heptane Using Four Imidazolium-Based Ionic Liquids
• Determination and Modeling of Solubility of 4-Aminobenzamide in Different Pure Solvents
• Experimental Data and Thermodynamics Modeling (PC-SAFT EoS) of the {CO2 + Acetone + Pluronic F-127} System at High Pressures
• 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
• Vapor Liquid Equilibrium Data for 2,3-Pentanedione + (Acetaldehyde or Acetone) at (100, 150, and 200) kPa
• Measurement and Correlation of the Solubility of 2-Cyanoacetamide in 14 Pure Solvents and the Mixing Properties of Solutions
• Solubility, Model Correlation, and Solvent Effect of 2-Amino-3-methylbenzoic Acid in 12 Pure Solvents
• Solubility and Solution Thermodynamics of 3-Nitrophthalonitrile in 12 Neat Solvents at Temperatures from 278.15 to 323.15 K
• Solubility Measurement, Correlation, and Molecular Interactions of 3-Methyl-6-nitroindazole in Different Neat Solvents and Mixed Solvents from T = 278.15 to 328.15 K
• Equilibrium Solubility, Model Correlation, and Solvent Effect of Indole-3-acetic Acid in Twelve Pure Solvents
• Measurement and Correlation of Solubility of Calcium Formate (Form alpha) in Different Binary Solvent Mixtures at Temperatures from 283.15 to 323.15 K
• Determination and Correlation of Solubility of Borneol, Camphor, and Isoborneol in Different Solvents
• Solubility Study of (2E)-1-(3-Pyridyl)-3-(dimethylamino)-2-propen-1-one in Different Pure Solvents and Binary Solvent Mixtures from 278.15 to 328.15 K
• Experimental Measurements of the {CO2 (1) + Acetone (2) + Ivermectin (3)} System at High Pressure
• Solubility Determination and Thermodynamic Modeling of 2-Mercaptobenzimidazole in 12 Solvents from T = 278.15 K to T = 318.15 K
• Solubility Measurement and Thermodynamic Model Correlation of 5-Nitrosalicylaldehyde in Different Solvents
• o-Nitrophenylacetonitrile Solubility in Several Pure Solvents: Measurement, Correlation, and Solvent Effect Analysis
• Measurement and Correlation of Solubilities of 5,5'-Dinitramino-3,3'-bi[1,2,4-triazolate] Carbohydrazide Salt (CBNT) in Various Pure Solvents and a Binary Mixture (Dimethyl Sulfoxide + Water) from 298.15 to 343.15 K
• 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
• Solubility Measurement and Correlation of 2-Oxindole in 12 Pure Organic Solvents
• Solubility of d-Aspartic Acid in Several Neat Solvents: Determination, Modeling, and Solvent Effect Analysis
• Assessment of Pyrrolidinium-Based Ionic Liquid for the Separation of Binary Mixtures Based on Activity Coefficients at Infinite Dilution
• Solubility Measurement and Phase Equilibrium Modeling of 2-Aminobenzamide in 15 Pure Solvents
• Measurement of the Solubility of Diclazuril and Discussion of the Effect of the Cosolvent
• Solubility Determination, Modeling, and Thermodynamic Dissolution Properties of Benzenesulfonamide in 16 Neat Solvents from 273.15 to 324.45 K
• Solid-Liquid Equilibrium Solubility, Thermodynamic Properties, and Molecular Simulation of Phenylphosphonic Acid in 15 Pure Solvents at Different Temperatures
• Determination and Correlation of Solubilities of 1,3,5-Trifluoro-2,4,6-triiodobenzene in Different Solvents from 289.25 to 332.15 K
• Solubility Determination, Correlation, and Solute-Solvent Molecular Interactions of 5-Aminotetrazole in Various Pure Solvents
• Solubility Determination and Thermodynamic Mixing Properties of 5-Methyl-2-pyrazinecarboxylic Acid in Different Solvents
• Solubility and Thermodynamic Modeling of Sulfanilamide in 12 Mono Solvents and 4 Binary Solvent Mixtures from 278.15 to 318.15 K
• Solubility 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
• Measurement and Correlation of Solubility of Marbofloxacin in 12 Pure Solvents from 283.15 to 328.15 K
• Solubility and Solvent Effect of 1-(2-Bromo-phenyl)-pyrrole-2,5-dione in 14 Pure Solvents from 278.15 to 323.15 K
• 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 Measurement and Modeling of 3-Hydroxy-2-nitropyridine in Ten Pure Solvents and Two Binary Mixed Solvents for T = (278.15-318.15) K
• Solubility and Thermodynamic Modeling of Dimethyl Terephthalate in Pure Solvents and the Evaluation of the Mixing Properties of the Solutions
• Solubility Determination of 2-Chloronicotinic Acid and Analysis of Solvent Effect
• Measurement and Correlation of the Solubility of Dienogest in Twelve Pure and Water + Methanol Binary Solvents at Temperatures from 273.15 to 318.15 K
• Solubility and Data Correlation of b-Arbutin in Different Monosolvents from 283.15 to 323.15 K
• Solubility Behavior and Data Modeling of l-Proline in Different Neat and Binary Solvent Systems
• Solid-Liquid Phase Equilibrium and Thermodynamic Analysis of N,N'-Diethylthiourea in Different Solvent Systems
• Thermodynamic Properties of Mixtures Containing Precursors of Vitamin B5
• Surface Tension of Pure Liquids and Binary Liquid Mixtures
• Excess Molar Enthalpies for Binary Mixtures of Ethanol + Acetone, + Octane, + Cyclohexane and 1-Propanol + Acetone, + Octane, + Heptane at 323.15
• Experimental Densities and Excess Volumes for Binary Mixtures Containing Propionic Acid, Acetone and Water from 283.15 K to 323.15 K at Atmospheric Pressure
• Liquid-Liquid Equilibria of Water + Benzonitrile + Propanone, or + Dimethylsulfoxide
• Measurement of Activity Coefficients of Solutes at Infinite Dilution in (Dimethyl Sulfoxide + Acetamide, or Formamide, or Urea) Using Gas Liquid Chromatography at the Temperature 298.15 K
• Surface Tension and Interfacial Tension of Binary Organic Liquid Mixtures
• Conductivities and Viscosities of the Ionic Liquid [bmim][PF6] + Water + Ethanol and [bmim][PF6] + Water + Acetone Ternary Mixtures
• Phase Behavior, Densities, and Isothermal Compressibility of CO2 + Pentane and CO2 + Acetone Systems in Various Phase Regions
• Measurement of Henry s Law Constants for Acetone, 2-Butanone, 2,3-Butanedione, and Isobutyraldehyde Using a Horizontal Flow Reactor
• Phase Behavior, Densities and Isothermal Compressibility of CO2 + Pentane + Acetone Ternary System in Various Phase Regions
• Excess Molar Volumes and Surface Tensions of Xylene with Acetone or 2-Butanone at 298.15 K
• Densities and Viscosities of Binary Liquid Mixtures of Trichloroethylene and Tetrachloroethylene with Some Polar and Nonpolar Solvents
• Density, Viscosity, and Excess Properties of Binary Liquid Mixtures of Propylene Carbonate with Polar and Nonpolar Solvents
• Vapor Liquid Equilibrium for Binary System of 2-Propanol + 2-Ethoxy-2-methylpropane and Ethyl Ethanoate + 2-Ethoxy-2-methylpropane at 333 K and 2-Propanone + 2-Ethoxy-2-methylpropane at 323 K
• Densities and Excess Molar Volumes for Acetone + Propionic Acid + Water from (283.15 to 323.15) K at Atmospheric Pressure
• Pressure-Density-Temperature Behavior of CO2/Acetone, CO2/Toluene, and CO2/Monochlorobenzene Mixtures in the Near-Critical Region
• Solubility of 11r-Hydroxy-16r,17r-Epoxyprogesterone in Different Solvents between 283 K and 323 K
• Determination of Henry s Law Constants and Activity Coefficients at Infinite Dilution of Flavor Compounds in Water at 298 K with a Gas-Chromatographic Method
• Measurement of the Phase Behavior of the Ternary System Carbon Dioxide + Acetone + Phenanthrene
• Isobaric Vapor-Liquid Equilibrium of Acetone + Methanol System in the Presence of Calcium Bromide
• Measurement of Isobaric Vapor - Liquid Equilibria of Dimethyl Carbonate with Acetone, 2-Butanone and 2-Pentanone at 101.3 kPa and Density and Speed of Sound at 298.15 K
• Solubility of Propyl p-hydroxybenzoate in Supercritical Carbon Dioxide with and without Cosolvent
• Vapor Liquid Equilibrium for Binary System of 2-Propanol + 1,1-Diethoxyethane at 353 K and Ethyl ethanoate + 1,1-Diethoxyethane at 348 K and 2-Propanone + 1,1-Diethoxyethane at 328 K
• High-Pressure Vapor-Liquid Equilbria of Some Carbon Dioxide + Organic Binary Systems
• Measurement of Activity Coefficients at Infinite Dilution of Benzene, Toluene, Ethanol, Esters, Ketones, and Ethers at Various Temperatures in Water Using the Dilutor Technique
• Vapor-Liquid Equilibria of the Carbon Dioxide + Acetone System at Pressures from (2.36 to 11.77) MPa and Temperatures from (333.15 to 393.15) K
• Solubility of DL-p-hydroxyphenylglycine Sulfate in Binary Acetone + Water Solvent Mixtures
• Solubility of Aspirin in Supercritical Carbon Dioxide with and without Acetone
• Densities, Refractive indices and Viscosities for Binary and Ternary Mixtures of Acetone, Ethanol and 2,2,4-Trimethylpentane at T = (288.15, 298.15, and 308.15) K
• Isothermal and Isobaric Vapor-Liquid Equilibria of the Ternary System of 2,2-Dimethoxypropane + Acetone + Methanol
• Solubility of Puerarin in Water, Ethanol, and Acetone from (288.2 to 328.2) K
• Solubility of Lovastatin in Acetone, Methanol, Ethanol, Ethyl Acetate, and Butyl Acetate between 283 K and 323 K
• Ternary Diffusion Coefficients of Glycerol + Acetone + Water by Taylor Dispersion Measurements at 298.15 K
• Solubility of Erythritol in Different Solvents
• Dynamic Viscosities of the Binary Systems Cyclohexane and Cyclopentane with Acetone, Butanone, or 2-Pentanone at Three Temperatures T ) (293.15, 298.15, and 303.15) K
• Solubility of 16.alpha.,17.alpha.-Epoxyprogesterone in Six Different Solvents
• Solubility of Ceftriaxone Disodium in Acetone, Methanol, Ethanol, N,N-Dimethylformamide, and Formamide between 278 and 318 K
• Solubility of p-Nitrobenzoic Acid in Supercritical Carbon Dioxide with and without Cosolvents
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 8. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography
• Vapor Liquid Equilibrium for Six Binary Systems of C4-Hydrocarbons + 2-Propanone
• Solubility of Organic Systems Containing 1,4-Dioxan-2-one
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 9. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in Trimethyl-butylammonium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography and Static Method
• Solubilities of 2-(6-Oxido-6H-dibenz[c,e][1,2]oxaphosphorin-6-yl)-methanol in the Selected Solvents
• Liquid-Liquid Equilibrium of (Water + Acetone) with Cumene or r-Methylstyrene or Phenol at Temperatures of (323.15 and 333.15) K
• Solubility of Erythromycin A Dihydrate in Different Pure Solvents and Acetone + Water Binary Mixtures between 293 K and 323 K
• Activity Coefficients at Infinite Dilution in 1-Alkyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
• Solubility and Metastable Zone Width of 1-Keto-1,2,3,4-tetrahydro-6-methylcarbazole in Acetone
• Henry s Constants of 1-Alkanols and 2-Ketones in Salt Solutions
• Phase Boundaries of CO2 + Toluene, CO2 + Acetone, and CO2 + Ethanol at High Temperatures and High Pressures
• Measurement and Correlation of Solubilities of Luteolin in Organic Solvents at Different Temperatures
• Solubility and Melting Properties of Salicylic Acid
• Solubilities of Some Phosphaspirocyclic Compounds in Selected Solvents
• Vapor-Liquid Equilibrium for Binary Systems of Diacetyl with Methanol and Acetone
• Solubility and Melting Properties of Salicylamide
• Experimental Study of Thermodynamic Properties of Mixtures Containing Ionic Liquid 1-Ethyl-3-methylimidazolium Ethyl Sulfate Using Gas-Liquid Chromatography and Transpiration Method
• Diffusion Coefficients of Aromatic Compounds at Infinite Dilution in Binary Mixtures at 298.15 K
• Activity Coefficients at Infinite Dilution of Polar Solutes in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Ionic Liquids as Entrainers in Extractive Distillation: Isobaric Vapor-Liquid Equilibria for Acetone + Methanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate
• Solubility of 4-(3,4-Dichlorophenyl)-1-tetralone in Some Organic Solvents
• Solubility of Xylitol in Ethanol, Acetone, N,N-Dimethylformamide, 1-Butanol, 1-Pentanol, Toluene, 2-Propanol, and Water
• Solubilities of Triphenylphosphine in Ethanol, 2-Propanol, Acetone, Benzene, and Toluene
• Solubility of Acephate in Different Solvents from (292.90 to 327.60) K
• Solubility of a-Carotene in Binary Solvents Formed by Some Hydrocarbons with 2,5,8-Trioxanonane, 2-Propanone, and Cyclohexanone
• Solubility of 3-Nitrophthalic Acid in Different Solvents between 278 K and 353 K
• Solubility of Clopidogrel Hydrogen Sulfate (Form II) in Different Solvents
• Measurement and Correlation of Griseofulvin Solubility in Different Solvents at Temperatures from (281.95 to 357.60) K
• Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Butyl-3-methyl-pyridinium Trifluoromethanesulfonate
• Solubilities of Nizatidine in Water, Methanol, Ethanol, Acetone, and Ethyl Acetate from (273.15 to 343.15) K
• Solubility of Artemisinin in Different Single and Binary Solvent Mixtures Between (284.15 and 323.15) K and NRTL Interaction Parameters
• Solubility of Anthracene in C1-C3 Alcohols from (298.2 to 333.2) K and Their Mixtures with 2-Propanone at 298.2 K
• Solubility of Sulpiride in Pure Organic Solvents between (278 and 333) K
• Excess Molar Enthalpies of CO2 + Acetone at Pressures from (9.00 to 18.00) MPa and Temperatures from (313.15 to 333.15) K
• Densities and Excess Molar Volumes for Binary Mixtures of Ionic Liquid 1-Ethyl-3-methylimidazolium Ethylsulfate with Solvents
• Solubility of Physalin D in Ethanol, Methanol, Propanone, Trichloromethane, Ethyl Ethanoate, and Water at Temperatures from (283.2 to 313.2) K
• Solubilities of Ibuprofen in Different Pure Solvents
• Solubility of Decabromodiphenyl Ether in Different Solvents at (283.0 to 323.0) K
• Solubilities of Phosphorus-Containing Compounds in Selected Solvents
• Solubility of CO2 in Propanone, 1-Ethyl-3-methylimidazolium Tetrafluoroborate, and Their Mixtures
• 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
• Solubility of Form III Piracetam in a Range of Solvents
• Measurement and Correlation of Solubility of Cefuroxime Acid in Pure and Binary Solvents at Various Temperatures
• Determination of Activity Coefficients at Infinite Dilution of 35 Solutes in the Ionic Liquid, 1-Butyl-3-methylimidazolium Tosylate, Using Gas-Liquid Chromatography
• Activity Coefficients at Infinite Dilution for Hydrocarbons in Fatty Alcohols Determined by Gas-Liquid Chromatography
• High-Pressure Multiphase Behavior of the Ternary Systems (Ethene + Water + Acetone) and (Ethane + Water + Acetone)
• Solubility and Crystal Size of Sirolimus in Different Organic Solvents
• Solubility of Butyl Paraben in Methanol, Ethanol, Propanol, Ethyl Acetate, Acetone, and Acetonitrile
• Solubilities of N-[(4-Bromo-3,5-difluorine)-phenyl]maleimide in Pyridine, Acetone, Tetrahydrofuran, Ethanol, Trichloromethane, and Acetonitrile at Temperature between (285.00 and 350.15) K
• Solubility of Florfenicol in Different Solvents at Temperatures from (278 to 318) K
• Solubilities of (a,Z)-2-Amino-a-(methoxyimino)-4-thiazoleethanethioic Acid S-2-Benzothiazolyl Ester in Different Pure Solvents and Binary Mixtures of Tetrahydrofuran + Dichloromethane or 1,2-Dichloroethane
• Solid Liquid Phase Equilibrium and Phase Diagram for the Ternary Carbamazepine Succinic Acid Ethanol or Acetone System at (298.15 and 308.15) K
• Influence of Typical Impurities on the Surface Tension Measurements of Binary Mixtures of Water and the Ionic Liquids 1-Butyl-3-Methylimidazolium Tetrafluoroborate and Chloride
• Solubilities of Phenylphosphinic Acid, Methylphenylphosphinic Acid, Hexachlorocyclotriphosphazene, and Hexaphenoxycyclotriphosphazene in Selected Solvents
• Activity Coefficients at Infinite Dilution in Methylimidazolium Nitrate Ionic Liquids
• Measurements of Activity Coefficients at Infinite Dilution for Organic Solutes and Water in the Ionic Liquid 1-Butyl-1-methylpiperydinium Thiocyanate
• Solubility of Candesartan Cilexetil in Different Solvents at Various Temperatures
• Measurement and Correlation for the Solubilities of Dihydrocapsaicin in n-Heptane, n-Hexane, n-Pentane, Ethyl Acetate, Acetone, Ethanol, and Water
• Critical Assessment of CO2 Solubility in Volatile Solvents at 298.15 K
• Solubilities of 3-Carboxy-3-hydroxypentanedioic Acid in Ethanol, Butan-1-ol, Water, Acetone, and Methylbenzene
• Measurement and Correlation for Solubilities of 16-Dehydropregnenolone Acetate in Different Solvents
• Solubility of CO2 in Alcohols, Glycols, Ethers, and Ketones at High Pressures from (288.15 to 318.15) K
• Measurement and Correlation for the Solubility of Dimethyl 1,4-Cyclohexanedione-2,5-dicarboxylate in Different Solvents at Temperatures from (278.15 to 323.15) K
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Butyl-3-methylimidazolium Nitrate Using Gas-Liquid Chromatography
• Solubility of 2-(2,4,6-Trichlorophenoxy)ethyl Bromide in Methanol, Ethanol, Propanol, Isopropanol, Acetonitrile, n-Heptane, and Acetone
• Solubilities of Tris(o-phenylenedioxy)cyclotriphosphazene in Selected Solvents
• Influence of Some Ionic Liquids Containing the Trifluoromethanesulfonate Anion on the Vapor Liquid Equilibria of the Acetone + Methanol System
• Thermodynamics of Ketone + Amine Mixtures. Part VIII. Molar Excess Enthalpies at 298.15 K for n-Alkanone + Aniline or + N-Methylaniline Systems
• Solubilities of Betulinic Acid in Thirteen Organic Solvents at Different Temperatures
• Interactions of Volatile Organic Compounds with the Ionic Liquid 1-Butyl-1-methylpyrrolidinium Dicyanamide
• Antisolvent Precipitation of Vitamin B6: A Thermodynamic Study
• 1-Ethyl-3-methylimidazolium Dicyanamide as a Very Efficient Entrainer for the Extractive Distillation of the Acetone + Methanol System
• Vapor Liquid Equilibrium Measurements of the Binary Mixtures Nitrogen + Acetone and Oxygen + Acetone
• Solubility of L-Phenylalanine Anhydrous and Monohydrate Forms: Experimental Measurements and Predictions
• Solubility of 6-Chloropyridazin-3-amine in Different Solvents
• Solubilities of 3-Methoxy-N-phenylaniline and 3-(Methylthio)-N-phenylaniline in Five Organic Solvents (285 K to 333.75 K)
• Solubility of Vitamin D3 in Six Organic Solvents at Temperatures from (248.2 to 273.2) K
• Crystal Structures, Reaction Rates, and Selected Physical Properties of Halo-Boronsubphthalocyanines (Halo = Fluoride, Chloride, and Bromide)
• Determination and Correlation of Pyridazin-3-amine Solubility in Eight Organic Solvents at Temperatures Ranging from (288.05 to 333.35) K
• Solubility of CO2 in Acetone, 1-Butyl-3-methylimidazolium Tetrafluoroborate, and Their Mixtures
• Measurement and Correlation of the Solubility of Febuxostat in Four Organic Solvents at Various Temperatures
• Solubility of the Metastable Polymorph of Piracetam (Form II) in a Range of Solvents
• Solubility of 2-Hydroxybenzoic Acid in Water, 1-Propanol, 2-Propanol, and 2-Propanone at (298.2 to 338.2) K and Their Aqueous Binary Mixtures at 298.2 K
• Determination and Correlation of Solubility Data and Dissolution Thermodynamic Data of l-Lactide in Different Pure Solvents
• Determination and Correlation of Solubility of Tris(3-hydroxypropyl)phosphine Oxide in Selected Solvents
• Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
• Solid Liquid Equilibria of Ternary 4-Nitro-2-benzofuran-1,3-dione + 5-Nitro-2-benzofuran-1,3-dione + 2-Propanone at 283.15 K and 323.15 K
• Solubilities of 4,4'-Dichlorodiphenyl Disulfide in Six Organic Solvents between (303.15 and 333.15) K
• Liquid Liquid Equilibrium for the Ternary System Acetone Oxime Methyl Ether Acetone Water
• Solubilities of Rutaecarpine in Twelve Organic Solvents from (283.2 to 323.2) K
• Solubility Measurement and Modeling for 2-Benzoyl-3-chlorobenzoic Acid and 1-Chloroanthraquinone in Organic Solvents
• Solubilities of 4-Bromo-1,8-naphthalic Anhydride in Different Pure Solvents and Binary Solvent Mixtures with the Temperature Range from (278.15 to 333.15) K
• Solubilities of 1,3,2-Dioxaphosphorinane-2-methanol-a,a-5,5-tetramethyl 2-oxide in Selected Solvents at 273.15 K to 343.15 K
• Solubilities of Phosphonic Acid, P,P'-(1,4-Piperazinediyl)bis-,P,P,P',P'-tetraphenyl Ester in Selected Solvents
• Solubility of Hesperetin in Mixed Solvents
• Vapor Liquid Equilibrium for the 1,1,1-Trifluorotrichloroethane + Sulfuryl Chloride System at 101.3 kPa
• Fluid Phase Behavior of Nitrogen + Acetone and Oxygen + Acetone by Molecular Simulation, Experiment and the Peng Robinson Equation of State
• Solubility and Dissolution Thermodynamic Data of Mefenamic Acid Crystals in Different Classes of Organic Solvents
• Measurement and Correlation of Solubility of Azithromycin Monohydrate in Five Pure Solvents
• Solubility of 1-Fluoro-4-(methylsulfonyl)benzene in Five Pure Organic Solvents at Temperatures from (288.40 to 331.50) K
• Solubilities of 4-(Hydroxymethyl)-1-oxido-2,6,7-trioxa-1-phosphabicyclo[2.2.2]octane in Organic Solvents
• Solubility of 4-Hydroxybenzaldehyde in Supercritical Carbon Dioxide with and without Cosolvents
• Dissociation Constants and Solubilities of Daidzein and Genistein in Different Solvents
• Solid Liquid Phase Equilibria of N,N'-[1,3-Phenylenebis(methylene)]bis(phosphoramidic acid) P,P,P',P'-Tetraphenyl Ester in 10 Pure Solvents
• Measurement and Correlation of Solubility and Dissolution Thermodynamic Properties of Furan-2-carboxylic Acid in Pure and Binary Solvents
• Measurement and Correlation for Solubility of L-valine in Water, Ethanol, N,N-Dimethylformamide, Acetone, and Isopropyl alcohol between 293.15 and 343.15 K
• Experimental Measurements and Modeling of the Solubility of Aceclofenac in Six Pure Solvents from (293.35 to 338.25) K
• Determination and Correlation of Solubility Data and Dissolution Thermodynamic Data of Cefixime Trihydrate in Seven Pure Solvents
• Measurement and Correlation of the Solubility of L-Carnitine in Different Pure Solvents and Ethanol Acetone Solvent Mixture
• Investigation of Surface Properties and Solubility of 1-Vinyl-3-alkyl/Esterimidazolium Halide Ionic Liquids by Density Functional Methods
• Measurement and Correlation of Solubility of l-Valine in Water + (Ethanol, N,N-Dimethylformamide, Acetone, Isopropyl Alcohol) from 293.15 K to 343.15 K
• 4-Amino-3,6-dichloropyridazine Solubility Measurement and Correlation in Seven Pure Organic Solvents from (278.15 to 333.15) K
• Solubility and Thermodynamic Functions of Isatin in Pure Solvents
• Solubility of Ibuprofen Sodium Dihydrate in Acetone + Water Mixtures: Experimental Measurement and Thermodynamic Modeling
• Measurement and Correlation of Solubility of Calcium-l-lactate Pentahydrate in Ethanol + Water and Acetone + Water Systems
• Phase equilibrium study of binary and ternary mixtures of ionic liquids + acetone + methanol
• Solubilities of 1,1'-[1,2-Ethanediylbis(oxy-1,2-ethanediyl)]bis-[3-methyl-1H-imidazolium-1-yl] Dihexafluorophosphate in Water, Methanol, Ethanol, Dimethylformamide, Dimethyl Sulfoxide, and (Acetone + Water) Binary Solvent Mixtures
• Liquid-liquid equilibria for the system acetone + solketal + glycerol at 303.2, 313.2 and 323.2 K
• Solubility of Two Polymorphs of Erlotinib Hydrochloride in Isopropanol and Acetone from (273.15 to 303.15) K
• Solubilities of Adipic Acid and Succinic Acid in Glutaric Acid + Acetone or n-butanol Mixture
• Isobaric Vapor Liquid Equilibrium for Acetone + Methanol + Phosphate Ionic Liquids
• Solubilities of 1,3,2-Dioxaphosphorinane-2-methanol-a,5,5-trimethyl-a-phenyl-2-oxide in Selected Solvents between 278.15 K and 343.15 K
• Thermodynamic Models for Determination of the Solubility of Sulfanilic Acid in Different Solvents at Temperatures from (278.15 to 328.15) K
• Solution Thermodynamics of Imidazolium-Based Ionic Liquids and Volatile Organic Compounds: Benzene and Acetone
• Solubility and Solution Thermodynamics of Diphenoxylate in Different Pure Solvents
• Determination and Correlation of Solubilities of 2-Isopropylthioxanthone (ITX) in Seven Different Solvents from (299.15 to 329.85) K
• Solubility of 3,3'-(Oxidi-2,1-ethanediyl)bis[1-methyl-imidazolium] Dihexafluorophosphate in Water, Methanol, Ethanol, Acetone, and Acetonitrile and Binary Mixtures (Water + DMF) from (283.00 to 323.00) K
• Solubility of 2,5-Di-tert-butylhydroquinone and Process Design for Its Purification Using Crystallization
• Solid Liquid Phase Equilibrium of Phosphoramidic acid, N,N'-1,2-Ethanediylbis-P,P,P',P'-tetraphenyl Ester in Selected Solvents
• Solubility Determination and Thermodynamic Models for 2-Methylnaphthalene in Different Solvents from T = (278.15 to 303.15) K
• Liquid Liquid Equilibrium for the Ternary System of Water + Acetone + Dihydromyrcenol at 358 K to 368 K under 0.8 MPa
• Experimental Investigation of the Solubility of CO2 in (Acetone + Water)
• Solubility of KCl and MgCl2 in Binary Solvents Formed by Acetone and Water in the Temperature Range between (293.15 and 323.15) K
• Surface Tension of the Ternary System Water + Acetone + Toluene
• Solubility of a-Sitosteryl Maleate and Stigmasteryl Maleate in Acetone and Ethyl Acetate
• Solubilities of 2,4,8,10-Tetraoxa-3,9-diphosphaspiro[5.5]undecane-3,9-dimethanol, r,r,rcents,rcents-tetramethyl-3,9-dioxide in Selected Solvents
• Solubilities of Betulin in Fourteen Organic Solvents at Different Temperatures
• Solubility of Flavonoids in Organic Solvents
• Measurement and Correlation of Solubility of Xylitol in Binary Ethanol + Acetone Solvent Mixtures with the Combined Nearly Ideal Binary Solvent/ Redlich-Kister Equation
• Solubility of 1-H-Tetrazole-1-acetic Acid in Different Solvents between 283 K and 323 K
• Solubility of Cyclotrimethylenetrinitramine (RDX) in Binary Solvent Mixtures
• Solubility of Irbesartan (Form A) in Different Solvents between 278 K and 323 K
• Solubility of Oleanolic Acid in Various Solvents from (288.3 to 328.3) K
• Ionic Conductivity of Selected 2:1 Electrolytes in Dilute Solutions of Mixed Aqueous Organic Solvents at 298.15 K
• Solubility of Imidacloprid in Different Solvents
• Solubilities of 2-(6-Oxido-6H-dibenz[c,e][1,2]oxaphosphorin-6-yl)-1,4-dihydroxy Phenylene in the Selected Solvents
• Experimental Determination of Solubilities of Betulin in Acetone + Water and Ethanol + Water Mixed Solvents at T ) (278.2, 288.2, 298.2, 308.2, and 318.2) K
• Solubility of 2-(4-Ethylbenzoyl)benzoic Acid in Eleven Organic Solvents between 279.55 K and 343.15 K
• Solubility of Tetrahydroxybenzophenone (THBP) in Acetone
• Solubility of Dioxopromethazine Hydrochloride in Different Solvents
• Solubility of Trimethoprim (TMP) in Different Organic Solvents from (278 to 333) K
• Diffusion Coefficients of Organic Compounds at Infinite Dilution in Mixtures Involving Associating Compounds. Experimental Determination and Modeling by Group Contribution Methods
• Activity Coefficients at Infinite Dilution of Polar Solutes in 1-Butyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas Liquid Chromatography
• Solubility of Acetylsalicylic Acid in Ethanol, Acetone, Propylene Glycol, and 2-Propanol
• Vapor Liquid Equilibrium for Binary Systems of 2,3-Pentanedione with Diacetyl and Acetone
• Isobaric Vapor Liquid Equilibria for Binary Systems of Acetone + Isopropenyl Acetate, 2-Butanone + Isopropenyl Acetate, and Isopropenyl Acetate + Acetylacetone at 101.3 kPa
• Solubility of p-Methylbenzene Sulfonic Acid in Pure and Modified Supercritical Carbon Dioxide
• Activity Coefficients at Infinite Dilution of Polar Solutes in 1-Propyl-2,3-dimethylimidazolium Tetrafluoroborate Using Gas Liquid Chromatography
• Density, Speed of Sound, and Derived Thermodynamic Properties of Ionic Liquids [EMIM]+[BETI]- or ([EMIM]+[CH3(OCH2CH2)2OSO3]- + Methanol or + Acetone) at T = (298.15 or 303.15 or 313.15) K
• Solubilities of Stearic Acid in Organic Solvents and in Azeotropic Solvent Mixtures
• Solubilities of Adefovir Dipivoxil in Different Binary Solvents at 298.15 K
• Solubility of Rifapentine in Different Organic Solvents
• Solubilities of Diphenylphosphinic Acid in Selected Solvents
• solubility of L-(+)-ascorbic acid in water, ethanol, methanol, propan-2-ol, acetone, acetonitrile, ethyl acetate, and tetrahydrofuran from (293 to 323) K
• Solubility of Lovastatin in Acetone + Water Solvent Mixtures
• Solubility of Hesperetin in Various Solvents from (288.2 to 323.2) K
• Densities and Viscosities of 1-Butyl-3-methylimidazolium Tetrafluoroborate + Molecular Solvent Binary Mixtures
• Solubility of Lovastatin in Ethyl Acetate, Propyl Acetate, Isopropyl Acetate, Butyl Acetate, sec-Butyl Acetate, Isobutyl Acetate, tert-Butyl Acetate, and 2-Butanone, between (285 and 313) K
• Solubility of Isoniazid in Various Organic Solvents from (301 to 313) K
• Solubility of 11 -Hydroxypregna-1,4,16-triene-3,20-dione in Different Solvents
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Ethyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Solubility of 1,6,6-Trimethyl-6,7,8,9-tetrahydrophenanthro[1,2-b]furan-10,11-dione in Four Organic Solvents from (283.2 to 323.3) 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
• Solubility of Diamantane, Trimantane, Tetramantane, and Their Derivatives in Organic Solvents
• Solubility of KBr in Binary Solvents Formed by Acetone and Water in the Temperature Range between (288.15 and 313.15) K
• Vapor-Liquid Phase Boundaries of Binary Mixtures of Carbon Dioxide with Ethanol and Acetone
• Solubilities of 1,4-Naphthoquinone in Acetone, Toluene, Xylene, Ethanol, and n-Butyl Alcohol
• Measurement and Correlation of Solubilities of trans-Resveratrol in Ethanol + Water and Acetone + Water Mixed Solvents at Different Temperatures
• Solubility of Naphthalene in Isobutyl Acetate, n-Butyric Acid, Ethyl Acetate, N-Methyl Pyrrolidone, N,N-Dimethylformamide, and Tetrahydrofuran
• Solubility of Artemisinin in Seven Different Pure Solvents from (283.15 to 323.15) K
• Solubility of Enrofloxacin Sodium in Various Solvents at Various Temperatures
• Solubilities of Palmitic Acid in Pure Solvents and Its Mixtures
• Solubility of Desmosterol in Five Organic Solvents
• Solubility of Ammonium Thiocyanate in Different Solvents
• Solubility of Fluorene in Benzene, Chloroform, Acetone, 1-Propanol, Isobutanol, and Methylbenzene from (283 to 323) K
• Solubility of Acenaphthene in Different Solvents from (283.00 to 323.00) K
• Solubility of Adipic Acid in Acetone, Chloroform, and Toluene
• Solubility of p-Aminobenzenesulfonamide in Supercritical Carbon Dioxide with Acetone Cosolvent
• Solubility of Podophyllotoxin in Six Organic Solvents from (283.2 to 323.2) K
• Solubility of Chloroquine Diphosphate and 4,7-Dichloroquinoline in Water, Ethanol, Tetrahydrofuran, Acetonitrile, and Acetone from (298.2 to 333.2) K
• Solubilities of Lauric Acid in n-Hexane, Acetone, Propanol, 2-Propanol, 1-Bromopropane, and Trichloroethylene from (279.0 to 315.3) K
• Solubility of Difloxacin in Acetone, Methanol, and Ethanol from (293.15 to 313.15) K
• Solubility of 2-Aminopyridine in Acetone, Chloroform, and Ethyl Acetate
• Solubility of Deflazacort in Binary Solvent Mixtures
• Solubility of Canthaxanthin in Pure Solvents from (293.15 to 343.15) K
• Solubility of (+)-(S)-2-(6-Methoxynaphthalen-2-yl) Propanoic Acid in Acetone, Methanol, Ethanol, Propan-2-ol, and Ethyl Ethanoate at Temperatures between (278 and 320) K
• Solubility and Metastable Zone of Cefoperazone Sodium in Acetone + Water System
• Solubility of Tiamulin Hydrogen Fumarate in Acetone, Acetonitrile, Ethyl Acetate, Ethyl Formate, and Butyl Acetate from (288.2 to 318.2) K
• Solubility of 3-Chlorophthalic Anhydride and 4-Chlorophthalic Anhydride in Organic Solvents and Solubility of 3-Chlorophthalic Acid and 4-Chlorophthalic Acid in Water from (283.15 to 333.15) K
• Solubilities of 1,1 -(Butane-1,4-diyl)-bis(pyridinium) Dihexafluorophosphate in Acetone + Water from (278.15 to 328.15) K
• Solubility of 3-Aminopyridine in Acetone + n-Butyl Acetate from (288.15 to 323.15) K
• Solubility of Butanedioic Acid in Different Solvents at Temperatures between 283 K and 333 K
• Solubility of p-Aminobenzenesulfonamide in Different Solvents from (283.15 to 323.15) K
• Solubilities of Triadimefon in Acetone + Water from (278.15 to 333.15) K
• Solubility of Fumaric Acid in Propan-2-ol, Ethanol, Acetone, Propan-1-ol, and Water
• Solubility of Thiotriazinone in Ethanol, 1-Propanol, 2-Propanol, 1-Butanol, Acetonitrile, Acetone, Ethyl Acetate, and Water from 293 K to 343 K
• Solubilities of Methyldiphenylphosphine Oxide in Selected Solvents
• Solubilities of Some Chlorophenols in Supercritical CO2 in the Presence and Absence of Cosolvents
• Solubilities of 3-Pentadecylphenol in Ethanol, 1-Butanol, Toluene, Acetone, Tetrachloromethane, and Ethyl Acetate
• Solubility of Captopril in 2-Propanol, Acetone, Acetonitrile, Methyl Acetate, Ethyl Acetate, and Butyl Acetate
• Solubilities of 3,9-Dimethyl-3,9-dioxide-2,4,8,10-tetraoxa-3,9-diphosphaspiro[5.5]undecane in Selected Solvents
• Solubility of Cytidine 5'-Diphosphocholine Sodium in Water and Different Binary Mixtures from (278.15 to 298.15) K
• Solubilities of 1,1-(Hexane-1,6-diyl)-bis(pyridinium) Dihexafluorophosphate in (Water + Acetone)
• Density and Viscosity of Ketones with Toluene at Different Temperatures and at Atmospheric Pressure
• Solubilities of 1,1'-(Ethane-1,2-diyl)-bis(pyridinium) Dihexafluorophosphate in Aqueous Acetone Mixtures
• Density and Viscosity of (2,2-Dichloro-N,N-di-2-propenylacetamide + Acetone) and (2,2-Dichloro-N,N-di-2-propenylacetamide + Ethanol) at T = (278.15 to 313.15) K
• Partial Molar Volumes of Butyltriethylammonium Iodide in Single Nonaqueous Solvents at 298.15 K
• Excess Enthalpies of Dibromomethane with Acetone, 1,4-Dioxane, Pyridine, Diethyl Ether, Ethyl Methyl Ketone, and Tetrahydrofuran at 303.15 K
• Solubility of Camellianin A in Methanol, Acetonitrile, Acetone, and Water from (283.2 to 313.2) K
• Density, Speed of Sound, and Refractive Index of 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate with Acetone, Methyl Acetate, and Ethyl Acetate at Temperatures from (278.15 to 328.15) K
• Experimental Measurement and Correlation of the Solubilities of 2,4-Dichloro-5-methoxypyrimidine in Ethyl Ethanoate, Methanol, Ethanol, Acetone, Tetrachloromethane, and Heptane at Temperatures between (295 and 320) K
• Solubility of 1,1'-(Ethane-1,2-diyl)-bis(3-methylpyridinium) Dihexafluorophosphate in Different Solvents
• Solubilities of 1,1?-(Propane-1,3-diyl)-bis(3-methyl-1H-imidazolium-1-yl) Dihexafluorophosphate in Different Solvents
• Activity Coefficients at Infinite Dilution of Polar Solutes in 1-(2-Hydroxyethyl)-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Henry s Law Constants of Organic Compounds in Water and n-Octane at T = 293.2 K
• Solubilities of (2,5-Dihydroxyphenyl)diphenyl Phosphine Oxide in Selected Solvents
• Solubilities of Sulfadiazine in Methanol, Ethanol, 1-Propanol, 2-Propanol, Acetone, and Chloroform from (294.15 to 318.15) K
• Solubility of Delphinidin in Water and Various Organic Solvents between (298.15 and 343.15) K
• 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
• ss-Sitosterol Solubility in Selected Organic Solvents
• Measurement and Modeling of Epigallocatechin Gallate Solubility in Supercritical Carbon Dioxide Fluid with Ethanol Cosolvent
• Solubility of 1,1'-(Butane-1,4-diyl)-bis(3-methylpyridinium) Dihexafluorophosphate in Different Solvents from (288.15 to 333.15) K
• Joback Method
• KDB
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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