Chemical Properties of Methyl Alcohol (CAS 67-56-1)

InChI

InChI=1S/CH4O/c1-2/h2H,1H3

InChI Key

OKKJLVBELUTLKV-UHFFFAOYSA-N

Formula

CH4O

SMILES

CO

Molecular Weight¹

32.04

CAS

67-56-1

Other Names

• Alcool methylique
• Alcool metilico
• Bieleski's solution
• CARBINOL
• CH3OH
• Colonial spirit
• Columbian spirit
• Columbian spirits
• Hydroxymethane
• METHANOL
• METHYLHYDROXIDE
• Metanolo
• Methyl hydroxide
• Methylalkohol
• Methylol
• Metylowy alkohol
• Monohydroxymethane
• NSC 85232
• Pyro alcohol
• Pyroxylic spirit
• Rcra waste number U154
• Spirit of wood
• UN 1230
• Wood alcohol
• Wood naphtha
• Wood spirit

• 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).
• LFL : Lower Flammability Limit (% in Air).
• UFL : Upper Flammability Limit (% in Air).
• T_flash,cc : Flash Point (Closed Cup Method) (K).
• T_flash,oc : Flash Point (Open Cup Method) (K).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• R_g : Radius of Gyration.
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• c_sound,fluid : Speed of sound in fluid (m/s).
• γ : Surface Tension (N/m).
• S°_{solid,1 bar} : Solid phase molar entropy at standard conditions (J/mol×K).
• T_boil : Normal Boiling Point Temperature (K).
• T_boil : Boiling point at given pressure (K).
• T_c : Critical Temperature (K).
• λ : Liquid thermal conductivity (W/m×K).
• α_diff : Thermal diffusivity (m²/s).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• V_c : Critical Volume (m³/kmol).
• V_m : Molar Volume (m³/mol).
• Z_c : Critical Compressibility.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Contents

1. Physical Properties
2. Temperature Dependent Properties
3. Pressure Dependent Properties
4. Datasets
5. Correlations
6. Similar Compounds
7. Mixtures
8. Sources

Physical Properties

Property	Value	Unit	Source
ω	0.5560		KDB
PAff	754.30	kJ/mol	NIST
Tig	737.04	K	KDB
BasG	724.50	kJ/mol	NIST
ΔcH°gas	-763.68 ± 0.20	kJ/mol	NIST
ΔcH°liquid	[-726.50; -713.83]	kJ/mol
ΔcH°liquid	-725.70 ± 0.10	kJ/mol	NIST
ΔcH°liquid	-726.50 ± 0.20	kJ/mol	NIST
ΔcH°liquid	-726.34 ± 0.20	kJ/mol	NIST
ΔcH°liquid	-715.05	kJ/mol	NIST
ΔcH°liquid	-713.83	kJ/mol	NIST
Cp,liquid	[80.81; 81.38]	J/mol×K
Cp,liquid	81.38	J/mol×K	Molar h...
Cp,liquid	80.81	J/mol×K	THERMOD...
μ	1.70	debye	KDB
η	[0.0005482; 0.0005500]	Pa×s
η	0.0005482	Pa×s	Densiti...
η	0.0005500	Pa×s	Densiti...
LFL	6.00	% in Air	KDB
UFL	36.50	% in Air	KDB
Tflash,cc	289.26	K	KDB
Tflash,oc	285.37	K	KDB
ΔfG°	-162.60	kJ/mol	KDB
Rg	1.5360		KDB
ΔfH°gas	-201.30	kJ/mol	KDB
ΔfH°liquid	[-251.30; -238.40]	kJ/mol
ΔfH°liquid	-238.40	kJ/mol	NIST
ΔfH°liquid	-239.50 ± 0.20	kJ/mol	NIST
ΔfH°liquid	-238.90 ± 3.60	kJ/mol	NIST
ΔfH°liquid	-250.60	kJ/mol	NIST
ΔfH°liquid	-251.30 ± 5.00	kJ/mol	NIST
ΔfusH°	2.43	kJ/mol	Joback Calculated Property
ΔvapH°	[35.30; 38.00]	kJ/mol
ΔvapH°	37.83	kJ/mol	NIST
ΔvapH°	37.80	kJ/mol	NIST
ΔvapH°	38.00	kJ/mol	NIST
ΔvapH°	37.40 ± 0.10	kJ/mol	NIST
ΔvapH°	37.43 ± 0.02	kJ/mol	NIST
ΔvapH°	37.43 ± 0.02	kJ/mol	NIST
ΔvapH°	37.30 ± 0.10	kJ/mol	NIST
ΔvapH°	37.30 ± 0.08	kJ/mol	NIST
ΔvapH°	37.70 ± 0.10	kJ/mol	NIST
ΔvapH°	37.40 ± 0.04	kJ/mol	NIST
ΔvapH°	37.80	kJ/mol	NIST
ΔvapH°	Outlier 35.30 ± 0.04	kJ/mol	NIST
IE	[10.82; 11.00]	eV
IE	10.84 ± 0.01	eV	NIST
IE	10.85 ± 0.03	eV	NIST
IE	10.82 ± 0.05	eV	NIST
IE	10.84 ± 0.07	eV	NIST
IE	10.90	eV	NIST
IE	10.84 ± 0.08	eV	NIST
IE	10.90 ± 0.03	eV	NIST
IE	10.85 ± 0.01	eV	NIST
IE	10.85 ± 0.00	eV	NIST
IE	10.90 ± 0.12	eV	NIST
IE	10.83 ± 0.03	eV	NIST
IE	10.85 ± 0.02	eV	NIST
IE	10.85	eV	NIST
IE	10.85	eV	NIST
IE	10.83 ± 0.01	eV	NIST
IE	10.85	eV	NIST
IE	10.83	eV	NIST
IE	10.84 ± 0.02	eV	NIST
IE	10.85	eV	NIST
IE	10.83	eV	NIST
IE	10.85 ± 0.02	eV	NIST
IE	10.96	eV	NIST
IE	Outlier 11.00	eV	NIST
IE	10.95	eV	NIST
IE	10.95	eV	NIST
IE	10.86	eV	NIST
IE	10.97 ± 0.03	eV	NIST
IE	10.96	eV	NIST
IE	10.95	eV	NIST
IE	10.94	eV	NIST
IE	10.95	eV	NIST
IE	10.96	eV	NIST
log10WS	[1.57; 1.57]
log10WS	1.57		Aq. Sol...
log10WS	1.57		Estimat...
logPoct/wat	-0.391		Crippen Calculated Property
McVol	30.820	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
NFPA Health	1		KDB
Pc	[8084.00; 8120.00]	kPa
Pc	8084.00	kPa	KDB
Pc	8120.00	kPa	Critica...
Inp	[330.00; 408.00]
Inp	340.00		NIST
Inp	384.00		NIST
Inp	356.00		NIST
Inp	336.00		NIST
Inp	373.00		NIST
Inp	355.00		NIST
Inp	Outlier 330.00		NIST
Inp	380.00		NIST
Inp	372.70		NIST
Inp	378.20		NIST
Inp	400.00		NIST
Inp	400.00		NIST
Inp	361.00		NIST
Inp	368.00		NIST
Inp	382.00		NIST
Inp	338.00		NIST
Inp	370.00		NIST
Inp	348.00		NIST
Inp	395.00		NIST
Inp	379.00		NIST
Inp	367.50		NIST
Inp	381.00		NIST
Inp	370.00		NIST
Inp	353.50		NIST
Inp	381.00		NIST
Inp	373.00		NIST
Inp	373.00		NIST
Inp	408.00		NIST
Inp	373.00		NIST
Inp	362.00		NIST
Inp	381.00		NIST
Inp	381.00		NIST
Inp	381.00		NIST
Inp	353.00		NIST
Inp	381.00		NIST
Inp	381.00		NIST
Inp	348.00		NIST
Inp	353.00		NIST
Inp	391.00		NIST
Inp	404.00		NIST
Inp	384.00		NIST
Inp	382.00		NIST
Inp	380.00		NIST
Inp	381.00		NIST
Inp	362.00		NIST
Inp	404.00		NIST
I	[860.00; 921.00]
I	917.00		NIST
I	891.00		NIST
I	Outlier 860.00		NIST
I	881.00		NIST
I	892.00		NIST
I	904.00		NIST
I	897.00		NIST
I	886.00		NIST
I	914.00		NIST
I	899.00		NIST
I	888.00		NIST
I	Outlier 869.00		NIST
I	910.40		NIST
I	916.00		NIST
I	Outlier 866.00		NIST
I	892.00		NIST
I	899.00		NIST
I	895.00		NIST
I	921.00		NIST
I	911.00		NIST
I	907.00		NIST
I	911.00		NIST
I	903.00		NIST
I	905.00		NIST
I	898.00		NIST
I	905.00		NIST
I	920.00		NIST
I	897.00		NIST
I	909.00		NIST
I	907.00		NIST
I	920.00		NIST
I	883.00		NIST
I	910.40		NIST
I	899.00		NIST
S°liquid	[126.80; 136.40]	J/mol×K
S°liquid	127.19	J/mol×K	NIST
S°liquid	126.80	J/mol×K	NIST
S°liquid	129.70	J/mol×K	NIST
S°liquid	136.40	J/mol×K	NIST
S°solid,1 bar	1.12	J/mol×K	NIST
Tboil	[337.45; 363.41]	K
Tboil	337.70	K	KDB
Tboil	337.50	K	Isobari...
Tboil	337.50	K	Isobari...
Tboil	337.75	K	Isobari...
Tboil	337.70	K	Isobari...
Tboil	337.86	K	Isobari...
Tboil	337.83	K	Experim...
Tboil	337.85	K	Measure...
Tboil	337.65	K	Isobari...
Tboil	337.65	K	Isobari...
Tboil	Outlier 363.41	K	Measure...
Tboil	337.65	K	Isobari...
Tboil	337.45	K	Measure...
Tboil	337.68	K	Experim...
Tboil	337.78	K	A new a...
Tboil	337.68	K	Isobari...
Tboil	337.85	K	Vapor L...
Tboil	337.85	K	Measure...
Tboil	337.45	K	Effect ...
Tboil	337.83	K	Isobari...
Tboil	337.68	K	Determi...
Tboil	337.83	K	Isobari...
Tboil	337.69	K	Isobari...
Tboil	337.83	K	Isobari...
Tboil	337.69	K	Vapor-L...
Tboil	337.62	K	Measure...
Tboil	337.67	K	Vapor-L...
Tboil	337.90	K	Vapor-L...
Tboil	337.75	K	Isobari...
Tboil	337.67	K	Vapor-L...
Tboil	337.57	K	Vapor-L...
Tboil	337.65	K	Isother...
Tboil	337.84	K	Organic...
Tboil	337.85	K	Isobari...
Tboil	337.84	K	Organic...
Tboil	337.85	K	Vapor L...
Tboil	337.75	K	Vapor L...
Tboil	337.82	K	Isobari...
Tboil	337.65	K	Experim...
Tboil	337.64	K	Vapor L...
Tboil	337.80	K	Effect ...
Tc	[505.20; 536.00]	K
Tc	512.50	K	KDB
Tc	512.30	K	Measure...
Tc	512.30	K	Measure...
Tc	512.50 ± 0.20	K	NIST
Tc	512.50	K	NIST
Tc	512.64	K	NIST
Tc	512.47 ± 0.10	K	NIST
Tc	512.50	K	NIST
Tc	512.64	K	NIST
Tc	512.60	K	NIST
Tc	512.50 ± 1.00	K	NIST
Tc	512.36 ± 0.15	K	NIST
Tc	512.36 ± 0.20	K	NIST
Tc	512.36 ± 0.20	K	NIST
Tc	514.70	K	NIST
Tc	512.65 ± 0.30	K	NIST
Tc	513.00	K	NIST
Tc	512.68	K	NIST
Tc	513.15 ± 2.77	K	NIST
Tc	513.90	K	NIST
Tc	513.20	K	NIST
Tc	505.20	K	NIST
Tc	512.60	K	NIST
Tc	513.80	K	NIST
Tc	513.20	K	NIST
Tc	513.20	K	NIST
Tc	513.40 ± 0.50	K	NIST
Tc	514.35 ± 1.00	K	NIST
Tc	515.20	K	NIST
Tc	513.40	K	NIST
Tc	Outlier 536.00	K	NIST
Tc	513.20	K	NIST
Tc	506.20	K	NIST
Tc	505.90	K	NIST
Tfus	[175.15; 175.47]	K
Tfus	175.47	K	KDB
Tfus	175.25	K	Aq. Sol...
Tfus	175.15	K	Solid-l...
Ttriple	[175.22; 176.00]	K
Ttriple	175.59	K	KDB
Ttriple	175.61 ± 0.05	K	NIST
Ttriple	175.59 ± 0.02	K	NIST
Ttriple	175.60 ± 0.10	K	NIST
Ttriple	175.37 ± 0.08	K	NIST
Ttriple	175.67 ± 0.20	K	NIST
Ttriple	175.22 ± 0.10	K	NIST
Ttriple	Outlier 176.00 ± 1.00	K	NIST
Ttriple	175.30 ± 0.10	K	NIST
Vc	[0.113; 0.118]	m3/kmol
Vc	0.117	m3/kmol	KDB
Vc	0.117	m3/kmol	NIST
Vc	0.113	m3/kmol	NIST
Vc	0.118 ± 0.004	m3/kmol	NIST
Vc	0.117 ± 0.004	m3/kmol	NIST
Zc	0.2219640		KDB
Zra	0.24		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[42.40; 66.80]	J/mol×K	[279.00; 585.35]
T(K) Ideal gas heat capacity (J/mol×K) 40 45 50 55 60 65 300 400 500
Cp,gas	42.40 ± 1.30	J/mol×K	279.00	NIST
Cp,gas	48.00 ± 1.30	J/mol×K	345.60	NIST
Cp,gas	46.80 ± 1.20	J/mol×K	347.35	NIST
Cp,gas	46.10 ± 1.30	J/mol×K	349.65	NIST
Cp,gas	47.60 ± 1.20	J/mol×K	356.55	NIST
Cp,gas	46.70 ± 1.30	J/mol×K	358.15	NIST
Cp,gas	48.20 ± 1.30	J/mol×K	358.85	NIST
Cp,gas	48.80 ± 1.30	J/mol×K	359.85	NIST
Cp,gas	50.30 ± 1.30	J/mol×K	368.15	NIST
Cp,gas	49.00 ± 1.20	J/mol×K	373.35	NIST
Cp,gas	51.30 ± 1.30	J/mol×K	382.15	NIST
Cp,gas	51.10 ± 1.20	J/mol×K	398.95	NIST
Cp,gas	52.30 ± 1.30	J/mol×K	401.15	NIST
Cp,gas	51.30 ± 1.20	J/mol×K	401.35	NIST
Cp,gas	52.01 ± 0.42	J/mol×K	403.20	NIST
Cp,gas	53.20 ± 1.30	J/mol×K	420.15	NIST
Cp,gas	53.90 ± 1.20	J/mol×K	431.45	NIST
Cp,gas	54.80 ± 1.20	J/mol×K	442.15	NIST
Cp,gas	55.90 ± 1.30	J/mol×K	442.65	NIST
Cp,gas	56.00 ± 1.20	J/mol×K	457.35	NIST
Cp,gas	57.20 ± 0.42	J/mol×K	464.00	NIST
Cp,gas	57.80 ± 1.20	J/mol×K	477.75	NIST
Cp,gas	58.40 ± 1.20	J/mol×K	485.05	NIST
Cp,gas	59.50 ± 1.20	J/mol×K	498.95	NIST
Cp,gas	60.40 ± 1.30	J/mol×K	521.20	NIST
Cp,gas	61.40 ± 1.20	J/mol×K	521.35	NIST
Cp,gas	64.30 ± 1.20	J/mol×K	555.95	NIST
Cp,gas	66.40 ± 1.20	J/mol×K	581.35	NIST
Cp,gas	66.80 ± 1.20	J/mol×K	585.35	NIST
Cp,liquid	[75.77; 206.35]	J/mol×K	[270.00; 512.78]
T(K) Liquid phase heat capacity (J/mol×K) 80 100 120 140 160 180 200 300 400 500
Cp,liquid	78.20	J/mol×K	270.00	NIST
Cp,liquid	75.77	J/mol×K	270.00	NIST
Cp,liquid	78.60	J/mol×K	283.15	Heat ca...
Cp,liquid	79.50	J/mol×K	288.15	Heat ca...
Cp,liquid	78.90	J/mol×K	288.15	NIST
Cp,liquid	79.90	J/mol×K	290.10	NIST
Cp,liquid	79.90	J/mol×K	292.00	NIST
Cp,liquid	80.80	J/mol×K	293.15	NIST
Cp,liquid	80.40	J/mol×K	293.15	Heat ca...
Cp,liquid	83.70	J/mol×K	298.00	NIST
Cp,liquid	83.30	J/mol×K	298.00	NIST
Cp,liquid	81.32	J/mol×K	298.00	NIST
Cp,liquid	81.13	J/mol×K	298.15	NIST
Cp,liquid	81.00	J/mol×K	298.15	NIST
Cp,liquid	81.17	J/mol×K	298.15	Thermod...
Cp,liquid	81.92	J/mol×K	298.15	NIST
Cp,liquid	81.30	J/mol×K	298.15	Heat ca...
Cp,liquid	81.47	J/mol×K	298.15	NIST
Cp,liquid	80.35	J/mol×K	298.15	NIST
Cp,liquid	81.56	J/mol×K	298.15	NIST
Cp,liquid	79.50	J/mol×K	298.15	NIST
Cp,liquid	81.11	J/mol×K	298.15	NIST
Cp,liquid	80.24	J/mol×K	298.15	NIST
Cp,liquid	80.22	J/mol×K	298.15	NIST
Cp,liquid	80.28	J/mol×K	298.15	NIST
Cp,liquid	85.80	J/mol×K	298.20	NIST
Cp,liquid	86.60	J/mol×K	300.80	NIST
Cp,liquid	82.30	J/mol×K	303.15	Heat ca...
Cp,liquid	83.40	J/mol×K	308.15	Heat ca...
Cp,liquid	83.01	J/mol×K	308.15	Thermod...
Cp,liquid	80.80	J/mol×K	311.00	NIST
Cp,liquid	84.50	J/mol×K	313.15	Heat ca...
Cp,liquid	83.56	J/mol×K	313.15	NIST
Cp,liquid	85.80	J/mol×K	313.20	NIST
Cp,liquid	85.70	J/mol×K	318.15	Heat ca...
Cp,liquid	85.51	J/mol×K	318.15	Thermod...
Cp,liquid	86.20	J/mol×K	323.00	NIST
Cp,liquid	87.00	J/mol×K	323.15	Heat ca...
Cp,liquid	88.64	J/mol×K	328.15	Thermod...
Cp,liquid	92.43	J/mol×K	338.15	Thermod...
Cp,liquid	96.88	J/mol×K	348.15	Thermod...
Cp,liquid	166.94	J/mol×K	512.35	Thermod...
Cp,liquid	184.24	J/mol×K	512.73	Thermod...
Cp,liquid	194.49	J/mol×K	512.77	Thermod...
Cp,liquid	202.18	J/mol×K	512.78	Thermod...
Cp,liquid	206.35	J/mol×K	512.78	Thermod...
Cp,solid	[5.40; 105.00]	J/mol×K	[20.50; 173.00]
Cp,solid	5.40	J/mol×K	20.50	NIST
Cp,solid	68.39	J/mol×K	120.00	NIST
Cp,solid	105.00	J/mol×K	173.00	NIST
η	[0.0003450; 0.0008699]	Pa×s	[278.15; 333.85]
T(K) Dynamic viscosity (Pa×s) 3.00e-4 4.00e-4 5.00e-4 6.00e-4 7.00e-4 8.00e-4 9.00e-4 280 300 320
η	0.0007418	Pa×s	278.15	Density...
η	0.0006890	Pa×s	283.15	Density...
η	0.0006781	Pa×s	283.15	Excess ...
η	0.0006315	Pa×s	288.15	Excess ...
η	0.0006410	Pa×s	288.15	Density...
η	0.0005910	Pa×s	293.00	Thermop...
η	0.0005930	Pa×s	293.15	Viscosi...
η	0.0005884	Pa×s	293.15	Excess ...
η	0.0005820	Pa×s	293.15	Densiti...
η	0.0005880	Pa×s	293.15	Propert...
η	0.0005770	Pa×s	293.15	Density...
η	0.0005850	Pa×s	293.15	Density...
η	0.0005870	Pa×s	293.15	Volumet...
η	0.0005810	Pa×s	293.15	Dynamic...
η	0.0005833	Pa×s	293.15	Viscosi...
η	0.0005950	Pa×s	293.15	Densiti...
η	0.0005676	Pa×s	293.15	Viscosi...
η	0.0005850	Pa×s	293.15	Dynamic...
η	0.0006075	Pa×s	293.15	Densiti...
η	0.0005840	Pa×s	293.15	Densiti...
η	0.0005990	Pa×s	293.15	Density...
η	0.0005320	Pa×s	298.15	Densiti...
η	0.0005510	Pa×s	298.15	Densiti...
η	0.0005585	Pa×s	298.15	Density...
η	0.0005530	Pa×s	298.15	Dynamic...
η	0.0005318	Pa×s	298.15	Viscosi...
η	0.0005446	Pa×s	298.15	Electri...
η	0.0008699	Pa×s	298.15	Volumet...
η	0.0005510	Pa×s	298.15	Viscosi...
η	0.0005450	Pa×s	298.15	Density...
η	0.0005500	Pa×s	298.15	Densiti...
η	0.0005470	Pa×s	298.15	Volumet...
η	0.0005510	Pa×s	298.15	Propert...
η	0.0005509	Pa×s	298.15	Excess ...
η	0.0005520	Pa×s	298.15	Densiti...
η	0.0005450	Pa×s	298.15	Dynamic...
η	0.0005770	Pa×s	298.15	Tempera...
η	0.0005560	Pa×s	298.15	Densiti...
η	0.0005520	Pa×s	298.15	Densiti...
η	0.0005580	Pa×s	298.15	Densiti...
η	0.0005130	Pa×s	302.45	Density...
η	0.0005180	Pa×s	303.00	Thermop...
η	0.0005090	Pa×s	303.15	Viscosi...
η	0.0005080	Pa×s	303.15	Dynamic...
η	0.0005070	Pa×s	303.15	Viscosi...
η	0.0005008	Pa×s	303.15	Viscosi...
η	0.0005261	Pa×s	303.15	Densiti...
η	0.0005130	Pa×s	303.15	Viscome...
η	0.0005140	Pa×s	303.15	Densiti...
η	0.0005120	Pa×s	303.15	Densiti...
η	0.0005154	Pa×s	303.15	Excess ...
η	0.0005100	Pa×s	303.15	Volumet...
η	0.0005240	Pa×s	303.15	Densiti...
η	0.0005150	Pa×s	303.15	Densiti...
η	0.0005060	Pa×s	303.15	Dynamic...
η	0.0005199	Pa×s	303.15	Density...
η	0.0005120	Pa×s	303.15	Density...
η	0.0005080	Pa×s	303.15	Density...
η	0.0005178	Pa×s	303.15	Densiti...
η	0.0005535	Pa×s	303.15	Densiti...
η	0.0005170	Pa×s	303.15	Propert...
η	0.0004760	Pa×s	308.15	Excess ...
η	0.0004840	Pa×s	308.15	Densiti...
η	0.0004849	Pa×s	308.15	Excess ...
η	0.0004860	Pa×s	308.15	Propert...
η	0.0004966	Pa×s	308.15	Densiti...
η	0.0005250	Pa×s	308.15	Tempera...
η	0.0004800	Pa×s	308.15	Viscome...
η	0.0004729	Pa×s	308.15	Viscosi...
η	0.0004900	Pa×s	308.15	Densiti...
η	0.0004780	Pa×s	308.15	Densiti...
η	0.0004650	Pa×s	308.15	Densiti...
η	0.0007287	Pa×s	308.15	Volumet...
η	0.0004930	Pa×s	308.15	Densiti...
η	0.0004747	Pa×s	308.15	Electri...
η	0.0004747	Pa×s	308.15	Electri...
η	0.0004843	Pa×s	308.15	Densiti...
η	0.0004760	Pa×s	308.15	Densiti...
η	0.0004857	Pa×s	308.15	Density...
η	0.0004500	Pa×s	313.00	Thermop...
η	0.0004470	Pa×s	313.15	Density...
η	0.0004430	Pa×s	313.15	Dynamic...
η	0.0004450	Pa×s	313.15	Densiti...
η	0.0004482	Pa×s	313.15	Viscosi...
η	0.0004559	Pa×s	313.15	Density...
η	0.0004480	Pa×s	313.15	Densiti...
η	0.0004450	Pa×s	313.15	Excess ...
η	0.0005010	Pa×s	313.15	Densiti...
η	0.0004440	Pa×s	313.15	Electri...
η	0.0004576	Pa×s	313.15	Excess ...
η	0.0004600	Pa×s	313.15	Propert...
η	0.0004500	Pa×s	313.15	Viscome...
η	0.0004410	Pa×s	313.15	Densiti...
η	0.0004702	Pa×s	313.15	Densiti...
η	0.0004470	Pa×s	313.15	Volumet...
η	0.0004490	Pa×s	313.15	Densiti...
η	0.0004590	Pa×s	313.15	Densiti...
η	0.0004515	Pa×s	313.15	Densiti...
η	0.0004438	Pa×s	313.15	Viscosi...
η	0.0004430	Pa×s	313.50	Density...
η	0.0004185	Pa×s	318.15	Electri...
η	0.0004324	Pa×s	318.15	Excess ...
η	0.0004259	Pa×s	318.15	Viscosi...
η	0.0005962	Pa×s	318.15	Volumet...
η	0.0004210	Pa×s	318.15	Densiti...
η	0.0004240	Pa×s	318.15	Densiti...
η	0.0004233	Pa×s	318.15	Densiti...
η	0.0004810	Pa×s	318.15	Tempera...
η	0.0004185	Pa×s	318.15	Electri...
η	0.0004390	Pa×s	318.15	Densiti...
η	0.0004220	Pa×s	318.15	Viscome...
η	0.0004210	Pa×s	318.15	Excess ...
η	0.0003950	Pa×s	323.15	Densiti...
η	0.0003950	Pa×s	323.15	Excess ...
η	0.0003873	Pa×s	323.15	Viscosi...
η	0.0003950	Pa×s	323.15	Densiti...
η	0.0004170	Pa×s	323.15	Densiti...
η	0.0003940	Pa×s	323.15	Volumet...
η	0.0003940	Pa×s	323.15	Densiti...
η	0.0003950	Pa×s	323.15	Densiti...
η	0.0004093	Pa×s	323.15	Excess ...
η	0.0004055	Pa×s	323.15	Viscosi...
η	0.0004601	Pa×s	323.15	Densiti...
η	0.0003970	Pa×s	323.15	Viscome...
η	0.0003860	Pa×s	323.55	Density...
η	0.0004430	Pa×s	328.15	Tempera...
η	0.0003720	Pa×s	328.15	Excess ...
η	0.0003872	Pa×s	328.15	Viscosi...
η	0.0003903	Pa×s	328.15	Excess ...
η	0.0004792	Pa×s	328.15	Volumet...
η	0.0003720	Pa×s	328.15	Densiti...
η	0.0003720	Pa×s	328.15	Densiti...
η	0.0003510	Pa×s	333.15	Densiti...
η	0.0003724	Pa×s	333.15	Excess ...
η	0.0003710	Pa×s	333.15	Viscosi...
η	0.0003490	Pa×s	333.15	Densiti...
η	0.0003450	Pa×s	333.85	Density...
ΔfusH	[0.59; 3.22]	kJ/mol	[157.30; 176.00]
T(K) Enthalpy of fusion at a given temperature (kJ/mol) 0.5 1 1.5 2 2.5 3 160 165 170 175
ΔfusH	0.64	kJ/mol	157.30	NIST
ΔfusH	0.59	kJ/mol	161.10	NIST
ΔfusH	3.18	kJ/mol	175.30	NIST
ΔfusH	3.18	kJ/mol	175.30	NIST
ΔfusH	3.22	kJ/mol	175.60	NIST
ΔfusH	2.20	kJ/mol	176.00	NIST
ΔvapH	[7.40; 43.70]	kJ/mol	[208.00; 510.00]
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 10 20 30 40 300 400 500
ΔvapH	43.70	kJ/mol	208.00	NIST
ΔvapH	39.20	kJ/mol	224.00	NIST
ΔvapH	38.90	kJ/mol	257.00	NIST
ΔvapH	38.40	kJ/mol	300.50	NIST
ΔvapH	38.70	kJ/mol	305.50	NIST
ΔvapH	37.00 ± 0.10	kJ/mol	306.00	NIST
ΔvapH	38.30	kJ/mol	312.50	NIST
ΔvapH	36.70 ± 0.10	kJ/mol	313.00	NIST
ΔvapH	38.30	kJ/mol	315.00	NIST
ΔvapH	36.20 ± 0.10	kJ/mol	321.00	NIST
ΔvapH	38.30	kJ/mol	322.50	NIST
ΔvapH	36.20 ± 0.10	kJ/mol	323.00	NIST
ΔvapH	37.50	kJ/mol	326.00	NIST
ΔvapH	35.60 ± 0.10	kJ/mol	331.00	NIST
ΔvapH	35.60 ± 0.10	kJ/mol	333.00	NIST
ΔvapH	35.21	kJ/mol	337.70	NIST
ΔvapH	35.25	kJ/mol	337.80	KDB
ΔvapH	35.30 ± 0.10	kJ/mol	338.00	NIST
ΔvapH	35.20 ± 0.10	kJ/mol	338.00	NIST
ΔvapH	34.70 ± 0.10	kJ/mol	343.00	NIST
ΔvapH	37.00	kJ/mol	355.50	NIST
ΔvapH	37.00	kJ/mol	360.00	NIST
ΔvapH	32.70	kJ/mol	373.00	NIST
ΔvapH	36.90	kJ/mol	412.50	NIST
ΔvapH	36.10	kJ/mol	415.50	NIST
ΔvapH	36.30	kJ/mol	418.00	NIST
ΔvapH	28.10	kJ/mol	423.00	NIST
ΔvapH	20.60	kJ/mol	473.00	NIST
ΔvapH	35.10	kJ/mol	483.00	NIST
ΔvapH	7.40	kJ/mol	510.00	NIST
Pvap	[4.25; 1754.90]	kPa	[274.15; 433.15]
T(K) Vapor pressure (kPa) 0 500 1000 1500 300 350 400
Pvap	4.25	kPa	274.15	Vapor P...
Pvap	5.50	kPa	278.15	Vapor P...
Pvap	6.70	kPa	282.55	Thermop...
Pvap	7.41	kPa	283.15	Vapor P...
Pvap	13.00	kPa	293.15	Vapor P...
Pvap	13.30	kPa	293.75	Thermop...
Pvap	16.95	kPa	298.15	Vapor-P...
Pvap	17.00	kPa	298.15	Measuri...
Pvap	16.97	kPa	298.15	Thermod...
Pvap	16.96	kPa	298.15	Thermod...
Pvap	16.97	kPa	298.15	Vapor p...
Pvap	20.00	kPa	301.45	Thermop...
Pvap	21.88	kPa	303.15	Thermod...
Pvap	21.88	kPa	303.15	Thermod...
Pvap	21.90	kPa	303.15	Measuri...
Pvap	21.88	kPa	303.15	Vapor-P...
Pvap	21.93	kPa	303.15	Thermod...
Pvap	21.93	kPa	303.15	Thermod...
Pvap	21.86	kPa	303.15	Vapor P...
Pvap	21.88	kPa	303.15	Vapor p...
Pvap	26.70	kPa	307.35	Thermop...
Pvap	27.96	kPa	308.15	Thermod...
Pvap	27.90	kPa	308.15	Measuri...
Pvap	27.98	kPa	308.15	Vapor-P...
Pvap	27.96	kPa	308.15	Thermod...
Pvap	27.96	kPa	308.15	Vapor p...
Pvap	30.33	kPa	309.79	Vapor-L...
Pvap	33.30	kPa	311.85	Thermop...
Pvap	35.42	kPa	313.06	Vapor-L...
Pvap	35.27	kPa	313.07	Vapour ...
Pvap	35.43	kPa	313.15	Vapor P...
Pvap	35.60	kPa	313.15	Measuri...
Pvap	35.45	kPa	313.15	Thermod...
Pvap	35.52	kPa	313.15	Vapor-L...
Pvap	35.51	kPa	313.15	Vapor-P...
Pvap	35.44	kPa	313.15	Thermod...
Pvap	35.44	kPa	313.15	Vapor p...
Pvap	38.33	kPa	315.00	Isobari...
Pvap	40.00	kPa	315.73	Vapor-L...
Pvap	40.00	kPa	315.75	Isobari...
Pvap	40.00	kPa	315.75	Thermop...
Pvap	40.41	kPa	316.02	Vapor-L...
Pvap	43.97	kPa	318.00	Isobari...
Pvap	44.54	kPa	318.15	Thermod...
Pvap	44.54	kPa	318.15	Vapor p...
Pvap	44.86	kPa	318.15	Isother...
Pvap	44.59	kPa	318.15	Vapor-P...
Pvap	45.11	kPa	318.43	Vapor-L...
Pvap	46.70	kPa	319.05	Thermop...
Pvap	50.30	kPa	320.90	Vapor-L...
Pvap	50.29	kPa	321.00	Isobari...
Pvap	53.30	kPa	322.05	Thermop...
Pvap	53.33	kPa	322.15	Isobari...
Pvap	55.50	kPa	323.13	Vapor L...
Pvap	55.57	kPa	323.14	Isother...
Pvap	55.39	kPa	323.14	Vapor-L...
Pvap	55.58	kPa	323.15	Vapor p...
Pvap	55.30	kPa	323.15	Vapor-L...
Pvap	55.61	kPa	323.15	Isother...
Pvap	55.58	kPa	323.15	Thermod...
Pvap	55.78	kPa	323.15	Thermod...
Pvap	55.78	kPa	323.15	Thermod...
Pvap	55.65	kPa	323.15	Vapor-P...
Pvap	55.54	kPa	323.15	Vapor P...
Pvap	55.69	kPa	323.15	Vapor-L...
Pvap	57.36	kPa	324.00	Isobari...
Pvap	60.00	kPa	324.65	Thermop...
Pvap	60.00	kPa	324.92	Isobari...
Pvap	59.99	kPa	324.96	Vapor-L...
Pvap	65.28	kPa	326.95	Vapor-L...
Pvap	65.25	kPa	327.00	Isobari...
Pvap	66.70	kPa	327.25	Thermop...
Pvap	66.66	kPa	327.34	Isobari...
Pvap	68.94	kPa	328.15	Vapor-P...
Pvap	74.02	kPa	330.00	Isobari...
Pvap	79.99	kPa	331.73	Isobari...
Pvap	80.97	kPa	332.08	Vapor L...
Pvap	83.76	kPa	333.00	Isobari...
Pvap	85.00	kPa	333.15	Experim...
Pvap	84.72	kPa	333.15	Vapor-L...
Pvap	84.93	kPa	333.15	Vapor P...
Pvap	84.62	kPa	333.15	Vapor-P...
Pvap	85.40	kPa	333.42	Isother...
Pvap	89.50	kPa	334.56	Isother...
Pvap	93.32	kPa	335.57	Isobari...
Pvap	94.55	kPa	336.00	Isobari...
Pvap	98.66	kPa	336.98	Isobari...
Pvap	99.91	kPa	337.35	Measure...
Pvap	100.00	kPa	337.42	Influen...
Pvap	100.00	kPa	337.42	1-Ethyl...
Pvap	101.30	kPa	337.45	Measure...
Pvap	101.30	kPa	337.45	Effect ...
Pvap	101.30	kPa	337.57	Vapor-L...
Pvap	101.30	kPa	337.65	Isother...
Pvap	101.33	kPa	337.65	Experim...
Pvap	101.30	kPa	337.65	Isobari...
Pvap	101.33	kPa	337.68	Determi...
Pvap	101.30	kPa	337.68	Isobari...
Pvap	101.30	kPa	337.68	Experim...
Pvap	101.30	kPa	337.69	Isobari...
Pvap	101.30	kPa	337.75	Vapor L...
Pvap	101.00	kPa	337.75	Isobari...
Pvap	101.30	kPa	337.78	A new a...
Pvap	101.30	kPa	337.82	Isobari...
Pvap	101.30	kPa	337.83	Isobari...
Pvap	101.30	kPa	337.83	Isobari...
Pvap	101.32	kPa	337.84	Organic...
Pvap	101.32	kPa	337.84	Organic...
Pvap	101.32	kPa	337.85	Isobari...
Pvap	101.00	kPa	337.85	Vapor L...
Pvap	101.30	kPa	337.85	Measure...
Pvap	101.32	kPa	337.85	Vapor L...
Pvap	101.30	kPa	337.90	Vapor-L...
Pvap	106.47	kPa	339.00	Isobari...
Pvap	119.61	kPa	342.00	Isobari...
Pvap	120.90	kPa	342.17	Isother...
Pvap	124.80	kPa	343.06	Isother...
Pvap	125.74	kPa	343.15	Vapor P...
Pvap	125.65	kPa	343.15	Vapor L...
Pvap	134.07	kPa	345.00	Isobari...
Pvap	142.60	kPa	346.64	Isother...
Pvap	150.69	kPa	348.15	Measure...
Pvap	150.67	kPa	348.15	Measure...
Pvap	150.71	kPa	348.15	Measure...
Pvap	163.20	kPa	350.25	Isother...
Pvap	181.00	kPa	353.10	Experim...
Pvap	181.56	kPa	353.15	Vapor P...
Pvap	180.50	kPa	353.15	Vapor-L...
Pvap	182.61	kPa	353.15	Measure...
Pvap	181.00	kPa	353.17	Isother...
Pvap	181.70	kPa	353.27	Isother...
Pvap	202.70	kPa	356.35	Isother...
Pvap	221.30	kPa	358.91	Isother...
Pvap	241.40	kPa	361.45	Isother...
Pvap	256.27	kPa	363.15	Vapor P...
Pvap	255.90	kPa	363.19	Isother...
Pvap	261.60	kPa	363.85	Isother...
Pvap	267.00	kPa	364.47	Isother...
Pvap	268.10	kPa	364.50	Vapour ...
Pvap	267.50	kPa	364.51	Vapor L...
Pvap	267.30	kPa	364.52	Vapor-L...
Pvap	267.60	kPa	364.52	Vapor L...
Pvap	288.90	kPa	366.88	Isother...
Pvap	321.30	kPa	370.13	Isother...
Pvap	341.20	kPa	372.04	Isother...
Pvap	350.90	kPa	372.90	Isother...
Pvap	352.62	kPa	373.15	Measure...
Pvap	352.64	kPa	373.15	Measure...
Pvap	352.80	kPa	373.15	Vapor-L...
Pvap	354.35	kPa	373.15	Vapor P...
Pvap	352.70	kPa	373.15	Measure...
Pvap	385.40	kPa	375.89	Isother...
Pvap	400.41	kPa	377.15	Measure...
Pvap	480.82	kPa	383.15	Vapor P...
Pvap	604.68	kPa	391.15	Measure...
Pvap	635.00	kPa	393.10	Experim...
Pvap	641.27	kPa	393.15	Vapor P...
Pvap	641.30	kPa	393.15	Vapor-L...
Pvap	840.10	kPa	403.15	Vapor-L...
Pvap	841.83	kPa	403.15	Vapor P...
Pvap	1042.57	kPa	411.15	Measure...
Pvap	1087.30	kPa	413.15	Vapor-L...
Pvap	1089.15	kPa	413.15	Vapor P...
Pvap	1565.62	kPa	428.15	Measure...
Pvap	1754.90	kPa	433.15	Vapor-L...
n0	[1.31670; 1.33030]		[288.15; 323.15]
T(K) Refractive Index 1.32 1.32 1.32 1.32 1.32 1.33 1.33 1.33 290 300 310 320
n0	1.33030		288.15	Excess ...
n0	1.32890		293.00	Liquid-...
n0	1.32853		293.10	Vapor-L...
n0	1.32850		293.15	Measure...
n0	1.32870		293.15	A novel...
n0	1.33010		293.15	Solubil...
n0	1.32930		293.15	Liquid-...
n0	1.32870		293.15	Isother...
n0	1.32862		293.15	Liquid ...
n0	1.32860		293.15	Liquid ...
n0	1.32890		293.15	Isother...
n0	1.32880		293.15	Study o...
n0	1.32858		293.15	Synergi...
n0	1.32800		293.15	Experim...
n0	1.32860		293.15	Isobari...
n0	1.32850		293.15	Vapor-l...
n0	1.32850		293.15	Isobari...
n0	1.33010		293.15	Solubil...
n0	1.32870		293.15	Solubil...
n0	1.33010		293.15	Solubil...
n0	1.32843		293.15	Refract...
n0	1.32910		293.15	Measure...
n0	1.32900		293.20	Isobari...
n0	1.32640		298.10	PHYSICA...
n0	1.32640		298.15	Propert...
n0	1.32610		298.15	Mixing ...
n0	1.32649		298.15	Effect ...
n0	1.32700		298.15	Densiti...
n0	1.32720		298.15	Densiti...
n0	1.32648		298.15	Effect ...
n0	1.32690		298.15	Viscosi...
n0	1.32570		298.15	Applica...
n0	1.32655		298.15	Sucrose...
n0	1.32900		298.15	Volumet...
n0	1.32645		298.15	Excess ...
n0	1.32650		298.15	(Vapor ...
n0	1.32670		298.15	Binary ...
n0	1.32750		298.15	Isobari...
n0	1.32650		298.15	Excess ...
n0	1.32750		298.15	Excess ...
n0	1.32700		298.15	Tempera...
n0	1.32620		298.15	Experim...
n0	1.32634		298.15	Density...
n0	1.32687		298.15	Physica...
n0	1.32667		298.15	Density...
n0	1.32700		298.15	Excess ...
n0	1.32687		298.15	Physica...
n0	1.32660		298.15	Effect ...
n0	1.32610		298.15	Vapor-L...
n0	1.32630		298.15	Isobari...
n0	1.32660		298.15	Excess ...
n0	1.32640		298.15	Excess ...
n0	1.32700		298.15	Vapor-L...
n0	1.32640		298.15	Excess ...
n0	1.32880		298.15	Investi...
n0	1.32620		298.15	Liquid ...
n0	1.32650		298.15	Density...
n0	1.32650		298.15	Activit...
n0	1.32640		298.15	(Liquid...
n0	1.32640		298.15	Effect ...
n0	1.32668		298.15	Isother...
n0	1.32680		298.20	Isobari...
n0	1.32552		303.15	Densiti...
n0	1.32550		303.15	Experim...
n0	1.32433		303.15	Refract...
n0	1.32362		308.15	Densiti...
n0	1.32540		308.15	Excess ...
n0	1.32171		313.15	Densiti...
n0	1.32015		313.15	Refract...
n0	1.31670		323.15	Refract...
ρl	[752.83; 866.84]	kg/m3	[273.00; 333.15]
T(K) Liquid Density (kg/m3) 760 780 800 820 840 860 280 300 320
ρl	800.00	kg/m3	273.00	Saturat...
ρl	809.77	kg/m3	273.15	Molar C...
ρl	807.18	kg/m3	276.15	Volumet...
ρl	806.25	kg/m3	277.15	Volumet...
ρl	805.40	kg/m3	278.15	Volumet...
ρl	805.10	kg/m3	278.15	Thermop...
ρl	805.11	kg/m3	278.15	Molar C...
ρl	800.45	kg/m3	283.15	Molar C...
ρl	800.71	kg/m3	283.15	Density...
ρl	801.08	kg/m3	283.15	Volumet...
ρl	801.44	kg/m3	283.15	Densiti...
ρl	800.64	kg/m3	283.15	Volumet...
ρl	800.67	kg/m3	283.15	Volumet...
ρl	800.62	kg/m3	283.15	Excess ...
ρl	801.25	kg/m3	283.15	Densiti...
ρl	795.99	kg/m3	288.15	Volumet...
ρl	796.00	kg/m3	288.15	Volumet...
ρl	796.13	kg/m3	288.15	Mass de...
ρl	796.09	kg/m3	288.15	Effect ...
ρl	796.04	kg/m3	288.15	The mol...
ρl	795.50	kg/m3	288.15	Tempera...
ρl	796.41	kg/m3	288.15	Excess ...
ρl	796.09	kg/m3	288.15	Volumet...
ρl	795.96	kg/m3	288.15	Volumet...
ρl	795.77	kg/m3	288.15	Molar C...
ρl	795.70	kg/m3	288.15	Thermop...
ρl	795.97	kg/m3	288.15	Thermod...
ρl	796.41	kg/m3	288.15	Volumet...
ρl	797.30	kg/m3	290.15	Density...
ρl	791.00	kg/m3	293.00	KDB
ρl	791.26	kg/m3	293.15	Volumet...
ρl	791.30	kg/m3	293.15	Volumet...
ρl	793.60	kg/m3	293.15	Investi...
ρl	791.72	kg/m3	293.15	Excess ...
ρl	791.34	kg/m3	293.15	A Volum...
ρl	791.20	kg/m3	293.15	(Liquid...
ρl	791.82	kg/m3	293.15	Isobari...
ρl	791.10	kg/m3	293.15	Measure...
ρl	791.87	kg/m3	293.15	Densiti...
ρl	791.71	kg/m3	293.15	Volumet...
ρl	792.60	kg/m3	293.15	Densiti...
ρl	792.07	kg/m3	293.15	Densiti...
ρl	791.41	kg/m3	293.15	Electro...
ρl	793.50	kg/m3	293.15	Density...
ρl	791.49	kg/m3	293.15	Volume ...
ρl	791.29	kg/m3	293.15	Volumet...
ρl	791.40	kg/m3	293.15	Effect ...
ρl	791.90	kg/m3	293.15	Effect ...
ρl	791.35	kg/m3	293.15	Propert...
ρl	791.62	kg/m3	293.15	Experim...
ρl	791.33	kg/m3	293.15	Density...
ρl	791.28	kg/m3	293.15	Viscosi...
ρl	791.34	kg/m3	293.15	Density...
ρl	791.55	kg/m3	293.15	Thermod...
ρl	791.24	kg/m3	293.15	Thermop...
ρl	792.20	kg/m3	293.15	Isobari...
ρl	792.12	kg/m3	293.15	Densiti...
ρl	791.35	kg/m3	293.15	The mol...
ρl	791.40	kg/m3	293.15	Volumet...
ρl	791.35	kg/m3	293.15	Thermod...
ρl	791.08	kg/m3	293.15	Molar C...
ρl	791.28	kg/m3	293.15	Speed o...
ρl	790.80	kg/m3	295.15	Density...
ρl	787.00	kg/m3	298.00	Saturat...
ρl	787.50	kg/m3	298.10	Activit...
ρl	786.58	kg/m3	298.15	Speed o...
ρl	791.00	kg/m3	298.15	Tie-Lin...
ρl	786.53	kg/m3	298.15	Volumet...
ρl	786.40	kg/m3	298.15	Bubble ...
ρl	786.40	kg/m3	298.15	Tempera...
ρl	786.56	kg/m3	298.15	Excess ...
ρl	786.42	kg/m3	298.15	Isother...
ρl	786.70	kg/m3	298.15	Liquid ...
ρl	786.60	kg/m3	298.15	Thermod...
ρl	786.61	kg/m3	298.15	Density...
ρl	786.71	kg/m3	298.15	Density...
ρl	786.55	kg/m3	298.15	Volumet...
ρl	786.00	kg/m3	298.15	Excess ...
ρl	786.61	kg/m3	298.15	Explora...
ρl	787.00	kg/m3	298.15	Solubil...
ρl	786.62	kg/m3	298.15	Tempera...
ρl	787.00	kg/m3	298.15	Phase d...
ρl	785.30	kg/m3	298.15	Volumet...
ρl	786.63	kg/m3	298.15	Partial...
ρl	786.62	kg/m3	298.15	Isother...
ρl	787.21	kg/m3	298.15	Densiti...
ρl	786.79	kg/m3	298.15	Volume ...
ρl	786.37	kg/m3	298.15	Molar C...
ρl	786.10	kg/m3	298.15	Liquid ...
ρl	786.64	kg/m3	298.15	Binary ...
ρl	786.57	kg/m3	298.15	Binary ...
ρl	786.61	kg/m3	298.15	Isobari...
ρl	787.20	kg/m3	298.15	Thermod...
ρl	786.74	kg/m3	298.15	Study o...
ρl	786.60	kg/m3	298.15	Probing...
ρl	786.40	kg/m3	298.15	Density...
ρl	786.68	kg/m3	298.15	Density...
ρl	866.84	kg/m3	298.15	Tempera...
ρl	786.62	kg/m3	298.15	Effect ...
ρl	786.88	kg/m3	298.15	Effect ...
ρl	787.00	kg/m3	298.15	Effect ...
ρl	786.66	kg/m3	298.15	Physica...
ρl	786.56	kg/m3	298.15	Vapor-l...
ρl	786.69	kg/m3	298.15	Volumet...
ρl	786.90	kg/m3	298.15	Cation ...
ρl	786.61	kg/m3	298.15	Partial...
ρl	786.62	kg/m3	298.15	Density...
ρl	787.00	kg/m3	298.15	Liquid-...
ρl	786.58	kg/m3	298.15	Ionic m...
ρl	786.67	kg/m3	298.15	Non-cov...
ρl	786.62	kg/m3	298.15	Experim...
ρl	786.44	kg/m3	298.15	Thermod...
ρl	786.20	kg/m3	298.15	Measure...
ρl	786.30	kg/m3	298.15	Solubil...
ρl	787.10	kg/m3	298.15	Isobari...
ρl	786.67	kg/m3	298.15	Propert...
ρl	787.52	kg/m3	298.15	Modifie...
ρl	786.59	kg/m3	298.15	Determi...
ρl	786.99	kg/m3	298.15	Excess ...
ρl	786.60	kg/m3	298.15	Measure...
ρl	786.62	kg/m3	298.15	Isobari...
ρl	786.59	kg/m3	298.15	Isobari...
ρl	786.60	kg/m3	298.15	Volumet...
ρl	786.20	kg/m3	298.15	Dynamic...
ρl	786.50	kg/m3	298.15	Density...
ρl	786.20	kg/m3	298.15	Measure...
ρl	786.60	kg/m3	298.15	Solubil...
ρl	786.59	kg/m3	298.15	Excess ...
ρl	786.56	kg/m3	298.15	Separat...
ρl	786.38	kg/m3	298.15	Partial...
ρl	786.80	kg/m3	298.15	Density...
ρl	786.30	kg/m3	298.15	Volumet...
ρl	786.56	kg/m3	298.15	Excess ...
ρl	791.81	kg/m3	298.15	Liquid-...
ρl	786.59	kg/m3	298.15	Ternary...
ρl	785.90	kg/m3	298.15	Solubil...
ρl	786.69	kg/m3	298.15	Isobari...
ρl	786.57	kg/m3	298.15	Liquid ...
ρl	786.97	kg/m3	298.15	Experim...
ρl	786.55	kg/m3	298.15	Thermod...
ρl	786.64	kg/m3	298.15	Thermod...
ρl	786.49	kg/m3	298.15	Refract...
ρl	787.35	kg/m3	298.15	Excess ...
ρl	786.58	kg/m3	298.15	Volumet...
ρl	786.50	kg/m3	298.15	Fully a...
ρl	786.46	kg/m3	298.15	Measure...
ρl	789.27	kg/m3	298.15	Investi...
ρl	786.59	kg/m3	298.15	Vapor P...
ρl	786.30	kg/m3	298.15	Thermod...
ρl	786.40	kg/m3	298.15	Liquid ...
ρl	786.67	kg/m3	298.15	Ebullio...
ρl	786.70	kg/m3	298.15	Liquid-...
ρl	786.30	kg/m3	298.15	Thermop...
ρl	787.01	kg/m3	298.15	Volumet...
ρl	786.58	kg/m3	298.15	Liquid ...
ρl	786.55	kg/m3	298.15	Liquid-...
ρl	786.55	kg/m3	298.15	Surface...
ρl	789.70	kg/m3	298.15	Phase e...
ρl	786.67	kg/m3	298.15	Density...
ρl	786.00	kg/m3	298.15	Ternary...
ρl	786.65	kg/m3	298.15	Electro...
ρl	786.59	kg/m3	298.15	Liquid ...
ρl	786.58	kg/m3	298.15	Volumet...
ρl	786.62	kg/m3	298.15	Experim...
ρl	786.60	kg/m3	298.15	Dynamic...
ρl	786.75	kg/m3	298.15	Mass de...
ρl	786.58	kg/m3	298.15	Volumet...
ρl	786.69	kg/m3	298.15	Effect ...
ρl	786.55	kg/m3	298.15	Liquid ...
ρl	786.62	kg/m3	298.15	Mutual ...
ρl	786.55	kg/m3	298.15	Volumet...
ρl	786.53	kg/m3	298.15	Volumet...
ρl	786.64	kg/m3	298.15	The mol...
ρl	786.50	kg/m3	298.15	Excess ...
ρl	787.43	kg/m3	298.15	Densiti...
ρl	786.80	kg/m3	298.15	Vapor-L...
ρl	796.00	kg/m3	298.20	Solubil...
ρl	791.00	kg/m3	298.20	Phase e...
ρl	786.27	kg/m3	298.20	Ternary...
ρl	786.00	kg/m3	303.00	Saturat...
ρl	781.85	kg/m3	303.15	Speed o...
ρl	782.07	kg/m3	303.15	Volume ...
ρl	781.83	kg/m3	303.15	Volumet...
ρl	783.40	kg/m3	303.15	Ternary...
ρl	781.86	kg/m3	303.15	Volumet...
ρl	781.97	kg/m3	303.15	Effect ...
ρl	781.96	kg/m3	303.15	Density...
ρl	781.85	kg/m3	303.15	Electro...
ρl	783.00	kg/m3	303.15	Densiti...
ρl	782.43	kg/m3	303.15	Densiti...
ρl	781.91	kg/m3	303.15	Densiti...
ρl	781.81	kg/m3	303.15	Excess ...
ρl	782.68	kg/m3	303.15	Densiti...
ρl	784.59	kg/m3	303.15	Investi...
ρl	782.40	kg/m3	303.15	Viscous...
ρl	782.24	kg/m3	303.15	Excess ...
ρl	781.91	kg/m3	303.15	Thermod...
ρl	781.91	kg/m3	303.15	The mol...
ρl	782.29	kg/m3	303.15	Volumet...
ρl	781.86	kg/m3	303.15	Volumet...
ρl	781.90	kg/m3	303.15	A Volum...
ρl	781.40	kg/m3	303.15	Density...
ρl	782.44	kg/m3	303.15	Thermod...
ρl	781.97	kg/m3	303.15	Volumet...
ρl	781.81	kg/m3	303.15	Isobari...
ρl	781.81	kg/m3	303.15	Thermop...
ρl	781.94	kg/m3	303.15	Propert...
ρl	782.16	kg/m3	303.15	Effect ...
ρl	781.65	kg/m3	303.15	Molar C...
ρl	781.89	kg/m3	303.15	Density...
ρl	782.75	kg/m3	303.15	Densiti...
ρl	781.81	kg/m3	303.15	Vapor-l...
ρl	782.00	kg/m3	303.15	Liquid ...
ρl	781.95	kg/m3	303.15	Physica...
ρl	783.40	kg/m3	303.15	Excess ...
ρl	782.61	kg/m3	303.15	Densiti...
ρl	777.10	kg/m3	308.15	Speed o...
ρl	776.90	kg/m3	308.15	Density...
ρl	777.18	kg/m3	308.15	Effect ...
ρl	777.20	kg/m3	308.15	Propert...
ρl	777.20	kg/m3	308.15	Physica...
ρl	777.20	kg/m3	308.15	Tempera...
ρl	777.56	kg/m3	308.15	Densiti...
ρl	777.14	kg/m3	308.15	Density...
ρl	777.15	kg/m3	308.15	Partial...
ρl	777.41	kg/m3	308.15	Effect ...
ρl	777.18	kg/m3	308.15	Non-cov...
ρl	777.21	kg/m3	308.15	Volumet...
ρl	777.45	kg/m3	308.15	Study o...
ρl	776.89	kg/m3	308.15	Molar C...
ρl	777.10	kg/m3	308.15	Density...
ρl	777.07	kg/m3	308.15	Thermod...
ρl	777.30	kg/m3	308.15	Density...
ρl	777.21	kg/m3	308.15	Density...
ρl	777.11	kg/m3	308.15	Volumet...
ρl	777.55	kg/m3	308.15	Volumet...
ρl	777.33	kg/m3	308.15	Volume ...
ρl	777.16	kg/m3	308.15	Thermod...
ρl	777.87	kg/m3	308.15	Investi...
ρl	776.90	kg/m3	308.15	Thermop...
ρl	777.21	kg/m3	308.15	Effect ...
ρl	777.10	kg/m3	308.15	Volumet...
ρl	776.95	kg/m3	308.15	Electro...
ρl	777.08	kg/m3	308.15	Volumet...
ρl	777.29	kg/m3	308.15	Mass de...
ρl	777.91	kg/m3	308.15	Densiti...
ρl	777.16	kg/m3	308.15	The mol...
ρl	777.10	kg/m3	308.15	Volumet...
ρl	779.00	kg/m3	313.00	Saturat...
ρl	772.31	kg/m3	313.14	Volumet...
ρl	772.32	kg/m3	313.15	Speed o...
ρl	772.70	kg/m3	313.15	Liquid ...
ρl	772.36	kg/m3	313.15	A Volum...
ρl	772.31	kg/m3	313.15	Density...
ρl	772.33	kg/m3	313.15	Volumet...
ρl	772.42	kg/m3	313.15	Propert...
ρl	772.37	kg/m3	313.15	Density...
ρl	772.55	kg/m3	313.15	Volume ...
ρl	772.44	kg/m3	313.15	Volumet...
ρl	771.97	kg/m3	313.15	Electro...
ρl	773.50	kg/m3	313.15	Densiti...
ρl	772.74	kg/m3	313.15	Excess ...
ρl	772.78	kg/m3	313.15	Volumet...
ρl	772.44	kg/m3	313.15	Effect ...
ρl	772.32	kg/m3	313.15	Excess ...
ρl	772.73	kg/m3	313.15	Excess ...
ρl	774.60	kg/m3	313.15	Ternary...
ρl	772.89	kg/m3	313.15	Thermod...
ρl	772.90	kg/m3	313.15	Densiti...
ρl	772.29	kg/m3	313.15	Thermop...
ρl	772.11	kg/m3	313.15	Molar C...
ρl	772.64	kg/m3	313.15	Effect ...
ρl	772.10	kg/m3	313.15	Density...
ρl	772.32	kg/m3	313.15	Volumet...
ρl	772.38	kg/m3	313.15	Thermod...
ρl	773.14	kg/m3	313.15	Densiti...
ρl	772.97	kg/m3	313.15	Densiti...
ρl	772.44	kg/m3	313.15	Investi...
ρl	772.38	kg/m3	313.15	The mol...
ρl	774.60	kg/m3	313.15	Excess ...
ρl	773.05	kg/m3	313.15	Densiti...
ρl	767.51	kg/m3	318.15	Speed o...
ρl	767.52	kg/m3	318.15	Volumet...
ρl	768.32	kg/m3	318.15	Densiti...
ρl	768.09	kg/m3	318.15	Thermod...
ρl	767.71	kg/m3	318.15	Mass de...
ρl	767.40	kg/m3	318.15	Thermop...
ρl	767.57	kg/m3	318.15	The mol...
ρl	767.84	kg/m3	318.15	Effect ...
ρl	767.74	kg/m3	318.15	Effect ...
ρl	767.70	kg/m3	318.15	Density...
ρl	767.52	kg/m3	318.15	Volumet...
ρl	767.97	kg/m3	318.15	Volumet...
ρl	767.20	kg/m3	318.15	Density...
ρl	767.74	kg/m3	318.15	Volume ...
ρl	768.01	kg/m3	318.15	Study o...
ρl	767.56	kg/m3	318.15	Density...
ρl	767.50	kg/m3	318.15	Density...
ρl	767.75	kg/m3	318.15	Non-cov...
ρl	768.04	kg/m3	318.15	Thermod...
ρl	767.74	kg/m3	318.15	Partial...
ρl	767.60	kg/m3	318.15	Volumet...
ρl	768.03	kg/m3	318.15	Densiti...
ρl	768.00	kg/m3	323.00	Saturat...
ρl	762.67	kg/m3	323.15	Speed o...
ρl	764.00	kg/m3	323.15	Densiti...
ρl	763.47	kg/m3	323.15	Densiti...
ρl	762.70	kg/m3	323.15	A Volum...
ρl	762.72	kg/m3	323.15	Density...
ρl	762.83	kg/m3	323.15	Thermop...
ρl	763.03	kg/m3	323.15	Effect ...
ρl	762.61	kg/m3	323.15	Vapor-l...
ρl	762.67	kg/m3	323.15	Volumet...
ρl	763.24	kg/m3	323.15	Thermod...
ρl	763.12	kg/m3	323.15	Volumet...
ρl	762.10	kg/m3	323.15	Density...
ρl	763.24	kg/m3	323.15	Densiti...
ρl	763.36	kg/m3	323.15	Densiti...
ρl	758.23	kg/m3	328.15	Volumet...
ρl	758.20	kg/m3	328.15	Excess ...
ρl	757.97	kg/m3	328.15	Mass de...
ρl	757.77	kg/m3	328.15	Volumet...
ρl	752.83	kg/m3	333.15	Volumet...
ρl	753.39	kg/m3	333.15	Densiti...
ρl	753.51	kg/m3	333.15	Densiti...
ρl	753.29	kg/m3	333.15	Volumet...
ρl	752.86	kg/m3	333.15	A Volum...
ΔfusS	[3.70; 18.30]	J/mol×K	[157.30; 176.00]
T(K) Entropy of fusion at a given temperature (J/mol×K) 4 6 8 10 12 14 16 18 160 165 170 175
ΔfusS	4.00	J/mol×K	157.30	NIST
ΔfusS	3.70	J/mol×K	161.10	NIST
ΔfusS	18.10	J/mol×K	175.30	NIST
ΔfusS	18.30	J/mol×K	175.60	NIST
ΔfusS	12.50	J/mol×K	176.00	NIST
csound,fluid	[1020.46; 1169.50]	m/s	[278.15; 323.15]
T(K) Speed of sound in fluid (m/s) 1050 1100 1150 280 300 320
csound,fluid	1169.50	m/s	278.15	Volumet...
csound,fluid	1135.85	m/s	288.15	Densiti...
csound,fluid	1136.34	m/s	288.15	Thermop...
csound,fluid	1135.49	m/s	288.15	Volumet...
csound,fluid	1134.45	m/s	288.15	Effect ...
csound,fluid	1126.20	m/s	290.65	Effect ...
csound,fluid	1127.69	m/s	290.65	Thermop...
csound,fluid	1117.95	m/s	293.15	Effect ...
csound,fluid	1119.49	m/s	293.15	Thermop...
csound,fluid	1118.91	m/s	293.15	Densiti...
csound,fluid	1111.28	m/s	295.65	Thermop...
csound,fluid	1109.77	m/s	295.65	Effect ...
csound,fluid	1101.58	m/s	298.15	Effect ...
csound,fluid	1102.68	m/s	298.15	Volumet...
csound,fluid	1102.98	m/s	298.15	Thermop...
csound,fluid	1102.62	m/s	298.15	Densiti...
csound,fluid	1102.29	m/s	298.15	Volumet...
csound,fluid	1104.60	m/s	298.15	Ultraso...
csound,fluid	1102.41	m/s	298.15	Apparen...
csound,fluid	1109.00	m/s	298.15	Densiti...
csound,fluid	1103.80	m/s	298.15	Compres...
csound,fluid	1101.24	m/s	298.15	Thermod...
csound,fluid	1094.69	m/s	300.65	Thermop...
csound,fluid	1093.44	m/s	300.65	Effect ...
csound,fluid	1092.00	m/s	303.15	Densiti...
csound,fluid	1085.45	m/s	303.15	Effect ...
csound,fluid	1086.37	m/s	303.15	Volumet...
csound,fluid	1086.03	m/s	303.15	Densiti...
csound,fluid	1086.46	m/s	303.15	Thermop...
csound,fluid	1086.37	m/s	303.15	Applica...
csound,fluid	1077.33	m/s	305.65	Effect ...
csound,fluid	1078.30	m/s	305.65	Thermop...
csound,fluid	1074.00	m/s	308.15	Densiti...
csound,fluid	1069.80	m/s	308.15	Densiti...
csound,fluid	1070.15	m/s	308.15	Thermop...
csound,fluid	1070.11	m/s	308.15	Applica...
csound,fluid	1069.78	m/s	308.15	Volumet...
csound,fluid	1070.11	m/s	308.15	Volumet...
csound,fluid	1069.19	m/s	308.15	Effect ...
csound,fluid	1061.07	m/s	310.65	Effect ...
csound,fluid	1062.07	m/s	310.65	Thermop...
csound,fluid	1053.96	m/s	313.15	Applica...
csound,fluid	1053.97	m/s	313.15	Thermop...
csound,fluid	1053.96	m/s	313.15	Volumet...
csound,fluid	1060.00	m/s	313.15	Densiti...
csound,fluid	1052.93	m/s	313.15	Effect ...
csound,fluid	1045.91	m/s	315.65	Thermop...
csound,fluid	1044.90	m/s	315.65	Effect ...
csound,fluid	1037.91	m/s	318.15	Applica...
csound,fluid	1037.91	m/s	318.15	Volumet...
csound,fluid	1036.74	m/s	318.15	Effect ...
csound,fluid	1037.71	m/s	318.15	Volumet...
csound,fluid	1037.93	m/s	318.15	Thermop...
csound,fluid	1028.60	m/s	320.65	Effect ...
csound,fluid	1029.90	m/s	320.65	Thermop...
csound,fluid	1020.46	m/s	323.15	Effect ...
csound,fluid	1021.99	m/s	323.15	Thermop...
γ	[0.02; 0.02]	N/m	[278.20; 343.15]
T(K) Surface Tension (N/m) 0.02 0.02 0.02 0.02 0.02 0.02 0.02 280 300 320 340
γ	0.02	N/m	278.20	Thermop...
γ	0.02	N/m	279.11	Measure...
γ	0.02	N/m	282.59	Measure...
γ	0.02	N/m	288.15	Physico...
γ	0.02	N/m	288.15	Surface...
γ	0.02	N/m	288.20	Thermop...
γ	0.02	N/m	288.30	Measure...
γ	0.02	N/m	293.15	Thermod...
γ	0.02	N/m	293.15	Density...
γ	0.02	N/m	293.20	KDB
γ	0.02	N/m	293.37	Measure...
γ	0.02	N/m	296.97	Measure...
γ	0.02	N/m	298.15	Effect ...
γ	0.02	N/m	298.15	Surface...
γ	0.02	N/m	298.15	Physico...
γ	0.02	N/m	298.20	Thermop...
γ	0.02	N/m	301.54	Measure...
γ	0.02	N/m	303.15	Measuri...
γ	0.02	N/m	303.15	Thermod...
γ	0.02	N/m	303.20	Investi...
γ	0.02	N/m	307.31	Measure...
γ	0.02	N/m	308.15	Effect ...
γ	0.02	N/m	308.15	Physico...
γ	0.02	N/m	308.15	Surface...
γ	0.02	N/m	308.20	Thermop...
γ	0.02	N/m	311.76	Measure...
γ	0.02	N/m	313.15	Measuri...
γ	0.02	N/m	313.15	Thermod...
γ	0.02	N/m	313.20	Investi...
γ	0.02	N/m	317.66	Measure...
γ	0.02	N/m	318.15	Surface...
γ	0.02	N/m	318.15	Effect ...
γ	0.02	N/m	318.20	Thermop...
γ	0.02	N/m	322.90	Measure...
γ	0.02	N/m	323.15	Measuri...
γ	0.02	N/m	323.15	Thermod...
γ	0.02	N/m	323.20	Investi...
γ	0.02	N/m	326.56	Measure...
γ	0.02	N/m	328.15	Effect ...
γ	0.02	N/m	330.01	Measure...
γ	0.02	N/m	333.15	Measuri...
γ	0.02	N/m	333.81	Measure...
γ	0.02	N/m	343.15	Measuri...
λ	0.19	W/m×K	298.15	Measure...

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboil	[315.70; 337.65]	K	[40.00; 96.60]
P(kPa) Boiling point at given pressure (K) 315 320 325 330 335 40 60 80
Tboil	315.70	K	40.00	Vapor-L...
Tboil	319.00	K	46.66	Vapor-L...
Tboil	324.30	K	58.80	Vapor-L...
Tboil	327.50	K	67.59	Vapor-L...
Tboil	330.60	K	76.13	Vapor-L...
Tboil	337.65	K	96.60	Low cos...

Datasets

1. Molar heat capacity at constant pressure, J/K/mol (2)
2. Viscosity, Pa*s (5)
3. Refractive index (Na D-line) (2)
4. Mass density, kg/m3 (10)
5. Speed of sound, m/s (2)
6. Thermal diffusivity, m2/s (1)
7. Molar volume, m3/mol (1)

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

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Molar heat capacity at constant pressure, J/K/mol - Liquid
248.15	500.00	74.02
248.15	1000.00	74.02
248.15	2500.00	73.95
248.15	5000.00	73.89
248.15	7500.00	73.79
248.15	10000.00	73.79
248.15	12500.00	73.76
273.15	500.00	77.03
273.15	1000.00	77.00
273.15	2500.00	76.93
273.15	5000.00	76.84
273.15	7500.00	76.80
273.15	10000.00	76.77
273.15	12500.00	76.74
298.15	500.00	81.39
298.15	1000.00	81.35
298.15	2500.00	81.19
298.15	5000.00	81.07
298.15	7500.00	81.03
298.15	10000.00	80.91
298.15	12500.00	80.91
323.15	500.00	86.87
323.15	1000.00	86.80
323.15	2500.00	86.64
323.15	5000.00	86.45
323.15	7500.00	86.29
323.15	10000.00	86.13
323.15	12500.00	86.00
348.15	500.00	93.66
348.15	1000.00	93.59
348.15	2500.00	93.43
348.15	5000.00	93.18
348.15	7500.00	92.92
348.15	10000.00	92.73
348.15	12500.00	92.41
373.15	500.00	101.83
373.15	1000.00	101.76
373.15	2500.00	101.41
373.15	5000.00	101.00
373.15	7500.00	100.64
373.15	10000.00	100.23
373.15	12500.00	99.97
398.15	1000.00	111.86
398.15	2500.00	111.28
398.15	5000.00	110.38
398.15	7500.00	109.58
398.15	10000.00	108.97
398.15	12500.00	108.33
423.15	2500.00	122.98
423.15	5000.00	121.41
423.15	7500.00	120.03
423.15	10000.00	118.84
423.15	12500.00	117.85
473.15	5000.00	162.32
473.15	7500.00	152.94
473.15	10000.00	146.91
473.15	12500.00	142.75
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Molar heat capacity at constant pressure, J/K/mol - Liquid
280.00	100.00	77.22
280.00	1000.00	74.02
280.00	5000.00	73.70
320.00	100.00	87.15
320.00	1000.00	85.87
320.00	5000.00	84.27
360.00	1000.00	97.41
360.00	5000.00	94.20
360.00	10000.00	94.52
360.00	15000.00	97.09
Reference

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
293.15	100.00	0.0006
293.15	20000.00	0.0006
293.15	40000.00	0.0007
293.15	60000.00	0.0008
293.15	80000.00	0.0008
293.15	100000.00	0.0009
313.15	100.00	0.0004
313.15	20000.00	0.0005
313.15	40000.00	0.0005
313.15	60000.00	0.0006
313.15	80000.00	0.0006
313.15	100000.00	0.0007
333.15	100.00	0.0003
333.15	20000.00	0.0004
333.15	40000.00	0.0004
333.15	60000.00	0.0005
333.15	80000.00	0.0005
333.15	100000.00	0.0005
353.15	20000.00	0.0003
353.15	40000.00	0.0003
353.15	60000.00	0.0004
353.15	80000.00	0.0004
353.15	100000.00	0.0004
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
298.15	81.50	0.0006
Reference

Fixed		Measured
Temperature, K - Gas	Amount density, mol/m3 - Gas	Viscosity, Pa*s - Gas
297.64	3.79	9.5940e-06
312.54	3.79	0.0000
324.75	3.79	0.0000
338.69	3.79	0.0000
352.91	3.79	0.0000
352.93	3.79	0.0000
366.84	3.79	0.0000
381.27	3.79	0.0000
395.39	3.79	0.0000
411.30	3.79	0.0000
423.50	3.79	0.0000
440.61	3.79	0.0000
468.85	3.79	0.0000
496.65	3.79	0.0000
525.41	3.79	0.0000
547.13	3.79	0.0000
569.26	3.79	0.0000
597.60	3.79	0.0000
298.16	6.32	9.5940e-06
312.25	6.32	0.0000
325.91	6.32	0.0000
339.77	6.32	0.0000
353.30	6.32	0.0000
355.50	6.32	0.0000
367.84	6.32	0.0000
382.15	6.32	0.0000
396.23	6.32	0.0000
411.31	6.32	0.0000
424.73	6.32	0.0000
440.07	6.32	0.0000
297.43	8.17	9.5510e-06
311.23	8.17	0.0000
325.15	8.17	0.0000
338.47	8.17	0.0000
352.62	8.17	0.0000
353.05	8.17	0.0000
366.82	8.17	0.0000
381.38	8.17	0.0000
394.76	8.17	0.0000
412.33	8.17	0.0000
423.31	8.17	0.0000
437.81	8.17	0.0000
496.40	8.17	0.0000
525.42	8.17	0.0000
546.79	8.17	0.0000
602.56	8.17	0.0000
297.41	10.1	9.5320e-06
313.89	10.1	0.0000
325.22	10.1	0.0000
338.62	10.1	0.0000
352.86	10.1	0.0000
353.44	10.1	0.0000
366.59	10.1	0.0000
380.86	10.1	0.0000
394.63	10.1	0.0000
409.51	10.1	0.0000
423.96	10.1	0.0000
437.60	10.1	0.0000
467.33	10.1	0.0000
496.56	10.1	0.0000
298.54	13.2	9.5790e-06
314.18	13.2	0.0000
325.76	13.2	0.0000
339.34	13.2	0.0000
353.22	13.2	0.0000
353.26	13.2	0.0000
367.10	13.2	0.0000
380.97	13.2	0.0000
395.40	13.2	0.0000
409.39	13.2	0.0000
423.77	13.2	0.0000
438.41	13.2	0.0000
467.74	13.2	0.0000
496.43	13.2	0.0000
526.39	13.2	0.0000
546.84	13.2	0.0000
567.40	13.2	0.0000
596.93	13.2	0.0000
301.53	17.93	9.6720e-06
311.12	17.93	9.9590e-06
325.59	17.93	0.0000
339.25	17.93	0.0000
353.58	17.93	0.0000
355.67	17.93	0.0000
366.93	17.93	0.0000
381.53	17.93	0.0000
395.23	17.93	0.0000
412.01	17.93	0.0000
424.38	17.93	0.0000
439.47	17.93	0.0000
468.08	17.93	0.0000
496.41	17.93	0.0000
527.99	17.93	0.0000
548.52	17.93	0.0000
571.83	17.93	0.0000
597.15	17.93	0.0000
299.92	24.58	9.6180e-06
310.88	24.58	9.9480e-06
325.98	24.58	0.0000
340.14	24.58	0.0000
353.71	24.58	0.0000
355.05	24.58	0.0000
368.03	24.58	0.0000
383.55	24.58	0.0000
395.18	24.58	0.0000
409.75	24.58	0.0000
424.41	24.58	0.0000
439.20	24.58	0.0000
466.95	24.58	0.0000
496.44	24.58	0.0000
526.84	24.58	0.0000
299.79	32.22	9.6020e-06
311.60	32.22	9.9690e-06
324.78	32.22	0.0000
338.66	32.22	0.0000
353.78	32.22	0.0000
355.04	32.22	0.0000
366.99	32.22	0.0000
381.92	32.22	0.0000
395.16	32.22	0.0000
410.18	32.22	0.0000
423.88	32.22	0.0000
439.16	32.22	0.0000
467.62	32.22	0.0000
496.97	32.22	0.0000
526.17	32.22	0.0000
547.30	32.22	0.0000
567.53	32.22	0.0000
597.12	32.22	0.0000
297.92	38.68	9.5550e-06
311.60	38.68	9.9710e-06
326.88	38.68	0.0000
338.72	38.68	0.0000
353.06	38.68	0.0000
353.18	38.68	0.0000
367.87	38.68	0.0000
381.90	38.68	0.0000
395.37	38.68	0.0000
410.35	38.68	0.0000
425.10	38.68	0.0000
441.61	38.68	0.0000
467.34	38.68	0.0000
496.21	38.68	0.0000
527.02	38.68	0.0000
547.49	38.68	0.0000
568.11	38.68	0.0000
598.60	38.68	0.0000
298.71	49.53	9.5760e-06
314.20	49.53	0.0000
324.77	49.53	0.0000
338.81	49.53	0.0000
352.35	49.53	0.0000
353.20	49.53	0.0000
367.81	49.53	0.0000
381.27	49.53	0.0000
394.88	49.53	0.0000
411.32	49.53	0.0000
423.52	49.53	0.0000
439.56	49.53	0.0000
467.49	49.53	0.0000
496.48	49.53	0.0000
525.14	49.53	0.0000
548.04	49.53	0.0000
569.93	49.53	0.0000
597.28	49.53	0.0000
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Viscosity, Pa*s - Liquid
101.00	297.80	0.0005
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Viscosity, Pa*s - Liquid
101.00	303.15	0.0005
Reference

Refractive index (Na D-line)

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Refractive index (Na D-line) - Liquid
100.00	298.15	1.3267
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Refractive index (Na D-line) - Liquid
298.15	100.00	1.3265
Reference

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.26	235.00	785.98
298.26	5000.00	790.69
298.26	9999.00	795.4
298.26	15013.00	799.88
298.26	19987.00	804.1
298.26	25008.00	808.17
298.26	29997.00	812.04
298.26	34991.00	815.76
298.26	39981.00	819.34
323.22	270.00	762.14
323.22	4990.00	767.53
323.22	9984.00	772.87
323.22	14982.00	777.91
323.22	19989.00	782.69
323.22	24986.00	787.21
323.22	29995.00	791.53
323.22	34987.00	795.64
323.22	39993.00	799.6
348.25	366.00	737.29
348.25	4987.00	743.46
348.25	9986.00	749.65
348.25	14991.00	755.42
348.25	20004.00	760.84
348.25	25020.00	765.94
348.25	30013.00	770.76
348.25	34989.00	775.32
348.25	40000.00	779.7
373.26	534.00	710.55
373.26	4983.00	717.67
373.26	9990.00	724.99
373.26	14998.00	731.69
373.26	19985.00	737.88
373.26	24994.00	743.68
373.26	29997.00	749.13
373.26	35001.00	754.27
373.26	39996.00	759.14
398.28	934.00	680.93
398.28	4984.00	689.0
398.28	9998.00	697.91
398.28	14986.00	705.88
398.28	19987.00	713.16
398.28	24992.00	719.87
398.28	29991.00	726.11
398.28	35005.00	731.99
398.28	40004.00	737.47
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	792.6
298.15	5000.00	796.2
298.15	9900.00	801.0
298.15	19700.00	808.4
298.15	29500.00	816.0
298.15	39300.00	823.8
298.15	49100.00	830.0
298.15	58900.00	836.3
323.15	100.00	770.3
323.15	5000.00	774.2
323.15	9900.00	778.2
323.15	19700.00	787.0
323.15	29500.00	795.0
323.15	39300.00	803.4
323.15	49100.00	811.0
323.15	58900.00	818.2
348.15	5000.00	748.9
348.15	9900.00	753.9
348.15	19700.00	764.1
348.15	29500.00	773.1
348.15	39300.00	782.6
348.15	49100.00	790.9
348.15	58900.00	798.9
373.15	5000.00	721.1
373.15	9900.00	727.7
373.15	19700.00	739.3
373.15	29500.00	750.4
373.15	39300.00	760.2
373.15	49100.00	769.6
373.15	58900.00	778.2
398.15	5000.00	690.0
398.15	9900.00	697.6
398.15	19700.00	712.8
398.15	29500.00	725.4
398.15	39300.00	736.0
398.15	49100.00	747.2
398.15	58900.00	757.0
423.15	5000.00	652.8
423.15	9900.00	665.2
423.15	19700.00	683.6
423.15	29500.00	698.8
423.15	39300.00	710.8
423.15	49100.00	723.9
423.15	58900.00	735.0
448.15	5000.00	610.4
448.15	9900.00	628.9
448.15	19700.00	652.4
448.15	29500.00	670.8
448.15	39300.00	685.6
448.15	49100.00	700.0
448.15	58900.00	713.0
473.15	5000.00	553.4
473.15	9900.00	585.0
473.15	19700.00	620.2
473.15	29500.00	642.0
473.15	39300.00	660.6
473.15	49100.00	677.2
473.15	58900.00	691.2
498.15	9900.00	525.0
498.15	19700.00	584.8
498.15	29500.00	613.4
498.15	39300.00	636.0
498.15	49100.00	655.0
498.15	58900.00	670.0
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.26	235.00	785.98
298.26	5000.00	790.69
298.26	9999.00	795.4
298.26	15013.00	799.88
298.26	19987.00	804.1
298.26	25008.00	808.17
298.26	29997.00	812.04
298.26	34991.00	815.76
298.26	39981.00	819.34
323.22	270.00	762.14
323.22	4990.00	767.53
323.22	9984.00	772.87
323.22	14982.00	777.91
323.22	19989.00	782.69
323.22	24986.00	787.21
323.22	29995.00	791.53
323.22	34987.00	795.64
323.22	39993.00	799.6
348.25	366.00	737.29
348.25	4987.00	743.46
348.25	9986.00	749.65
348.25	14991.00	755.42
348.25	20004.00	760.84
348.25	25020.00	765.94
348.25	30013.00	770.76
348.25	34989.00	775.32
348.25	40000.00	779.7
373.26	534.00	710.55
373.26	4983.00	717.67
373.26	9990.00	724.99
373.26	14998.00	731.69
373.26	19985.00	737.88
373.26	24994.00	743.68
373.26	29997.00	749.13
373.26	35001.00	754.27
373.26	39996.00	759.14
398.28	934.00	680.93
398.28	4984.00	689.0
398.28	9998.00	697.91
398.28	14986.00	705.88
398.28	19987.00	713.16
398.28	24992.00	719.87
398.28	29991.00	726.11
398.28	35005.00	731.99
398.28	40004.00	737.47
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
1000.00	303.20	783.0
2000.00	303.20	784.0
3000.00	303.20	785.0
4000.00	303.20	786.0
5000.00	303.20	787.0
6000.00	303.20	788.0
7000.00	303.20	788.9
8000.00	303.20	789.9
9000.00	303.20	790.9
10000.00	303.20	791.8
1000.00	323.20	762.8
2000.00	323.20	763.9
3000.00	323.20	765.0
4000.00	323.20	766.2
5000.00	323.20	767.3
6000.00	323.20	768.3
7000.00	323.20	769.4
8000.00	323.20	770.5
9000.00	323.20	771.5
10000.00	323.20	772.6
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	786.57
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	786.53
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
288.15	100.00	796.19
288.15	5000.00	800.57
288.15	10000.00	804.93
288.15	15000.00	808.85
288.15	20000.00	812.92
288.15	25000.00	816.56
288.15	30000.00	820.09
288.15	35000.00	823.62
288.15	40000.00	827.04
293.15	100.00	791.18
293.15	5000.00	795.97
293.15	10000.00	800.47
293.15	15000.00	804.52
293.15	20000.00	808.43
293.15	25000.00	812.34
293.15	30000.00	815.93
293.15	35000.00	819.32
293.15	40000.00	822.48
298.15	100.00	786.76
298.15	5000.00	791.52
298.15	10000.00	795.8
298.15	15000.00	800.13
298.15	20000.00	804.18
298.15	25000.00	808.04
298.15	30000.00	811.69
298.15	35000.00	815.2
298.15	40000.00	818.33
303.15	100.00	782.07
303.15	5000.00	786.79
303.15	10000.00	791.31
303.15	15000.00	795.85
303.15	20000.00	800.16
303.15	25000.00	804.08
303.15	30000.00	807.78
303.15	35000.00	811.31
303.15	40000.00	814.7
308.15	100.00	777.09
308.15	5000.00	781.85
308.15	10000.00	786.63
308.15	15000.00	791.23
308.15	20000.00	795.58
308.15	25000.00	799.85
308.15	30000.00	803.73
308.15	35000.00	807.42
308.15	40000.00	811.08
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	81.50	786.55
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.15	100.00	791.15
293.15	5000.00	795.92
293.15	10000.00	800.41
293.15	15000.00	804.64
293.15	20000.00	808.67
293.15	25000.00	812.52
293.15	30000.00	816.25
293.15	35000.00	819.89
303.15	100.00	781.84
303.15	5000.00	786.9
303.15	10000.00	791.61
303.15	15000.00	796.01
303.15	20000.00	800.14
303.15	25000.00	804.05
303.15	30000.00	807.78
303.15	35000.00	811.37
313.15	100.00	772.35
313.15	5000.00	777.48
313.15	10000.00	782.37
313.15	15000.00	786.99
313.15	20000.00	791.38
313.15	25000.00	795.59
313.15	30000.00	799.69
313.15	35000.00	803.73
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
100.00	283.15	800.54
100.00	293.15	791.23
100.00	298.15	786.51
100.00	303.15	781.96
100.00	313.15	772.43
100.00	318.15	767.47
100.00	323.15	762.78
100.00	328.15	757.83
100.00	333.15	752.96
2500.00	283.15	802.75
2500.00	293.15	793.52
2500.00	298.15	788.81
2500.00	303.15	784.36
2500.00	313.15	774.99
2500.00	318.15	770.09
2500.00	323.15	765.48
2500.00	328.15	760.61
2500.00	333.15	755.84
5000.00	283.15	804.88
5000.00	293.15	795.8
5000.00	298.15	791.18
5000.00	303.15	786.78
5000.00	313.15	777.53
5000.00	318.15	772.74
5000.00	323.15	768.2
5000.00	328.15	763.41
5000.00	333.15	758.73
10000.00	283.15	809.06
10000.00	293.15	800.17
10000.00	298.15	795.7
10000.00	303.15	791.48
10000.00	313.15	782.45
10000.00	318.15	777.79
10000.00	323.15	773.39
10000.00	328.15	768.75
10000.00	333.15	764.21
15000.00	283.15	813.06
15000.00	293.15	804.36
15000.00	298.15	800.02
15000.00	303.15	795.84
15000.00	313.15	787.08
15000.00	318.15	782.57
15000.00	323.15	778.3
15000.00	328.15	773.73
15000.00	333.15	769.39
20000.00	283.15	816.88
20000.00	293.15	808.39
20000.00	298.15	804.15
20000.00	303.15	799.97
20000.00	313.15	791.5
20000.00	318.15	787.09
20000.00	323.15	782.93
20000.00	328.15	778.49
20000.00	333.15	774.25
25000.00	283.15	820.6
25000.00	293.15	812.25
25000.00	298.15	808.1
25000.00	303.15	803.95
25000.00	313.15	795.74
25000.00	318.15	791.43
25000.00	323.15	787.34
25000.00	328.15	783.03
25000.00	333.15	778.87
30000.00	283.15	824.14
30000.00	293.15	815.94
30000.00	298.15	811.88
30000.00	303.15	807.83
30000.00	313.15	799.72
30000.00	323.15	791.56
30000.00	333.15	783.33
35000.00	283.15	827.58
35000.00	293.15	819.55
35000.00	298.15	815.52
35000.00	303.15	811.51
35000.00	313.15	803.62
35000.00	323.15	795.6
35000.00	333.15	787.53
Reference

Speed of sound, m/s

Operational condition: Frequency, MHz = 8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Speed of sound, m/s - Liquid
253.15	101.00	1259.391
253.15	5031.00	1283.569
253.15	10064.00	1307.272
253.15	15070.00	1329.88
253.15	20048.00	1351.494
253.15	25130.00	1372.789
253.15	30260.00	1393.514
273.15	101.00	1187.324
273.15	5017.00	1213.77
273.15	10158.00	1240.041
273.15	15070.00	1264.004
273.15	20132.00	1287.633
273.15	25155.00	1310.139
273.15	30074.00	1331.42
293.15	101.00	1119.106
293.15	5028.00	1147.798
293.15	10032.00	1175.493
293.15	15145.00	1202.422
293.15	20159.00	1227.564
293.15	25062.00	1251.109
293.15	30276.00	1275.096
313.15	101.00	1053.178
313.15	5046.00	1084.848
313.15	10127.00	1115.409
313.15	15085.00	1143.55
313.15	19989.00	1169.962
313.15	25090.00	1196.105
313.15	30009.00	1220.145
333.15	101.00	988.923
333.15	5029.00	1023.676
333.15	10110.00	1056.926
333.15	15215.00	1088.157
333.15	20093.00	1116.297
333.15	25061.00	1143.501
333.15	30122.00	1169.869
353.15	197.00	925.583
353.15	5097.00	963.758
353.15	10106.00	999.623
353.15	15143.00	1033.012
353.15	20216.00	1064.48
353.15	25221.00	1093.69
353.15	30092.00	1120.591
Reference

Operational condition: Frequency, MHz = 8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Speed of sound, m/s - Liquid
299.95	99.00	1096.3
220.38	100.00	1387.9
244.25	125.00	1294.5
349.98	201.00	935.8
244.27	761.00	1297.5
399.94	798.00	770.2
299.94	963.00	1101.7
349.98	970.00	941.9
399.94	1015.00	772.5
220.41	1023.00	1391.8
244.28	1200.00	1299.5
220.39	1839.00	1395.3
244.30	1980.00	1303.2
349.98	1998.00	949.9
399.94	2112.00	784.4
299.94	2240.00	1109.5
450.22	2562.00	568.3
349.98	4864.00	971.5
450.19	4910.00	608.8
244.31	5110.00	1317.8
399.93	5110.00	815.0
299.95	5128.00	1126.7
399.92	9339.00	854.2
500.06	9535.00	412.8
244.32	9712.00	1338.5
349.97	9858.00	1006.8
299.95	9896.00	1153.8
220.96	10454.00	1428.5
450.22	14312.00	730.4
499.98	19828.00	611.1
349.99	19881.00	1070.5
220.46	20095.00	1467.9
450.20	20347.00	794.1
299.96	21093.00	1212.5
399.92	21337.00	948.3
499.94	28092.00	708.5
500.06	30612.00	733.2
450.18	39568.00	943.1
499.94	40326.00	818.5
220.39	40357.00	1540.1
299.96	40780.00	1302.9
350.00	41608.00	1186.3
399.89	42375.00	1078.3
299.95	58877.00	1375.6
450.17	59905.00	1062.6
499.94	60313.00	955.4
349.95	60336.00	1270.3
220.26	60890.00	1606.5
399.90	61164.00	1172.4
220.38	69376.00	1631.5
220.37	69581.00	1632.2
450.20	72355.00	1124.9
299.94	80229.00	1452.1
399.91	81158.00	1258.6
349.96	82312.00	1356.2
399.93	84741.00	1273.4
399.73	98358.00	1325.1
299.95	98460.00	1511.3
349.96	99275.00	1415.9
220.37	111490.00	1746.8
399.91	122977.00	1409.6
299.96	123414.00	1585.5
349.97	124114.00	1495.1
Reference

Thermal diffusivity, m2/s

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Thermal diffusivity, m2/s - Liquid
0.00	299.15	9.7000e-08
370000.00	300.15	1.3500e-07
400000.00	299.85	1.3200e-07
860000.00	300.95	1.5700e-07
880000.00	299.15	1.5900e-07
1290000.00	301.05	1.7000e-07
1290000.00	301.05	1.6600e-07
1750000.00	300.75	1.8000e-07
2430000.00	299.15	1.8600e-07
3100000.00	299.15	1.9200e-07
3120000.00	299.15	1.9900e-07
4220000.00	298.15	2.1700e-07
5000000.00	299.75	2.3700e-07
5300000.00	297.95	2.1900e-07
Reference

Molar volume, m3/mol

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Molar volume, m3/mol - Liquid
298.15	100.00	0.0000
298.15	10000.00	0.0000
313.15	100.00	0.0000
313.15	10000.00	0.0000
328.15	100.00	0.0000
328.15	10000.00	0.0000
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 4027.94]	kPa	[257.16; 472.60]	The Yaw...
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.65992e+01
Coefficient B			-3.63914e+03
Coefficient C			-3.40540e+01
Temperature range, min.			257.16
Temperature range, max.			472.60
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 4000 300 350 400 450
Pvap	1.33	kPa	257.16	Calculated Property
Pvap	6.48	kPa	281.10	Calculated Property
Pvap	23.80	kPa	305.04	Calculated Property
Pvap	70.79	kPa	328.97	Calculated Property
Pvap	178.78	kPa	352.91	Calculated Property
Pvap	396.68	kPa	376.85	Calculated Property
Pvap	793.19	kPa	400.79	Calculated Property
Pvap	1456.93	kPa	424.72	Calculated Property
Pvap	2494.65	kPa	448.66	Calculated Property
Pvap	4027.94	kPa	472.60	Calculated Property
Pvap	[1.06e-04; 8099.01]	kPa	[175.47; 512.58]	KDB Vap...
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			7.90941e+01
Coefficient B			-7.02920e+03
Coefficient C			-9.37282e+00
Coefficient D			7.99273e-06
Temperature range, min.			175.47
Temperature range, max.			512.58
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 6000 7000 8000 200 300 400 500
Pvap	1.06e-04	kPa	175.47	Calculated Property
Pvap	0.02	kPa	212.93	Calculated Property
Pvap	0.78	kPa	250.38	Calculated Property
Pvap	9.61	kPa	287.84	Calculated Property
Pvap	61.07	kPa	325.30	Calculated Property
Pvap	251.59	kPa	362.75	Calculated Property
Pvap	771.81	kPa	400.21	Calculated Property
Pvap	1927.87	kPa	437.67	Calculated Property
Pvap	4162.73	kPa	475.12	Calculated Property
Pvap	8099.01	kPa	512.58	Calculated Property

Similar Compounds

Find more compounds similar to Methyl Alcohol.

Mixtures

• Benzene, chloro- + Methyl Alcohol
• Benzene, bromo- + Methyl Alcohol
• Dimethyl methylphosphonate + Methyl Alcohol
• Methyl Alcohol + Dimethyl phosphonate
• 2,6-Lutidine + Methyl Alcohol
• Pyridine, 2-methyl- + Methyl Alcohol
• Pyridine, 2,4,6-trimethyl- + Methyl Alcohol
• Isobutane + Methyl Alcohol
• Butane, 2-ethoxy-2-methyl- + Methyl Alcohol
• Butane, 2-ethoxy-2-methyl- + Methyl Alcohol + Water
• Carbonic acid, dimethyl ester + Methyl Alcohol
• Piperazine, 1-methyl- + Methyl Alcohol
• Pentane, 2-methyl- + Methyl Alcohol
• Cyclohexane, methyl- + Methyl Alcohol
• Formamide, N,N-dimethyl- + Pentane, 2-methyl- + Methyl Alcohol
• Formamide, N,N-dimethyl- + Cyclohexane, methyl- + Methyl Alcohol
• Benzene + Methyl Alcohol
• n-Hexane + Methyl Alcohol
• Butane, 2-methoxy-2-methyl- + Methyl Alcohol
• n-Hexane + Butane, 2-methoxy-2-methyl- + Methyl Alcohol

Find more mixtures with Methyl Alcohol.

Sources

• KDB Pure (Korean Thermophysical Properties Databank)
• KDB Vapor Pressure Data
• Crippen Method
• Dortmund Data Bank Vapor-Liquid Equilibrium Data
• High-Pressure Viscosity Measurements for the Ethanol + Toluene Binary System
• Thermodynamic Properties of Methanol in the Critical and Supercritical Regions
• Volumetric Properties of the Ionic Liquid, 1-Butyl-3-methylimidazolium Tetrafluoroborate, in Organic Solvents at T = 298.15 K
• Thermophysical Properties of Binary Mixtures of Methanol with Chlorobenzene and Bromobenzene from 293K to 313K
• Densities and Viscosities of Binary Mixtures of Methanol with Dimethyl Methylphosphonate and Dimethyl Phosphite from (293.15 to 333.15) K
• Viscosity of Associated Mixtures Approximated by the Grunberg-Nissan Model
• Volumetric Properties of Binary Mixtures of 2,4,6-Trimethylpyridine with 1,2-Ethanediol, Methanol, and Water, and the Association Energies of the O-H***N Bonded Complexes
• Solubility of Baicalein in Different Solvents from (287 to 323) K
• Liquid liquid equilibria for pseudoternary systems: isooctane benzene (methanol +water)
• 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
• Vapour liquid equilibrium for the 2-methylpropane + methanol, +ethanol, +2-propanol, +2-butanol and +2-methyl-2-propanol systems at 313.15K
• Isobaric vapor liquid equilibria for systems composed by 2-ethoxy-2-methylbutane, methanol or ethanol and water at 101.32 kPa
• Determination of activity coefficients at infinite dilution of organic solutes in the ionic liquid, trihexyl(tetradecyl)-phosphonium tris(pentafluoroethyl) trifluorophosphate, by gas liquid chromatography
• Measurements of isothermal vapor-liquid equilibrium of binary methanol/dimethyl carbonate system under pressure
• Viscosities and densities for binary mixtures of N-methylpiperazine with methanol, ethanol, n-propanol, iso-propanol, n-butanol and iso-butanol at 293.15, 298.15 and 303.15K
• Study of thermodynamic properties of binary solutions of lithium bromide or lithium chloride with methanol
• Thermodynamic properties of mixtures containing ionic liquids Vapor pressures and activity coefficients of n-alcohols and benzene in binary mixtures with 1-methyl-3-butyl-imidazolium bis(trifluoromethyl-sulfonyl) imide
• Solubility of aspirin in supercritical carbon dioxide/alcohol mixtures
• Measurement of infinite dilution activity coefficients of 1-alkanols (C1 C5) in water as a function of temperature (273 373 K)
• Enhancement of the anthracene aqueous solubility by a synergistic effect of alcohols and beta-cyclodextrin
• Liquid liquid equilibrium in ternary systems N,N-dimethylformamide + 2-methylpentane + methanol and N,N-dimethylformamide + methylcyclohexane + methanol
• Phase equilibria of methanol triolein system at elevated temperature and pressure
• Effect of temperature on the excess molar volumes of some alcohol + aromatic mixtures and modelling by cubic EOS mixing rules
• Vapour liquid equilibrium of octane enhancing additives in gasolines 7: Total pressure data and gE for the ternary mixture tert-amyl methyl ether (TAME), methanol and hexane at 313.15K
• Henry s law constants of propane, propene, butane, and 2-methylpropane in methanol at 374-490K
• Excess molar enthalpies for mixtures of carbon dioxide + a modifier (5 mol% methanol or 1-octanol) and hexane at 308.15K and 12.40MPa
• Vapor liquid liquid equilibria of perfluorohexane +CO2 + methanol, +toluene, and +acetone at 313K
• Effect of anion fluorination in 1-ethyl-3-methylimidazolium as solvent for the liquid extraction of ethanol from ethyl tert-butyl ether
• Viscous synergy and antagonism and isentropic compressibility of ternary mixtures containing 1,3-dioxolane, water and monoalkanols at 303.15K
• Activity coefficients of the binary mixtures of a-cresol or p-cresol with C l-C4 aliphatic alcohols near ambient pressure
• Volumetric behavior of water methanol mixtures in the vicinity of the critical region
• Liquid liquid equlibria of the system dimethyl carbonate + methanol +water at different temperatures
• Isothermal vapour liquid equilibrium with chemical reaction in the quaternary water + methanol + acetic acid + methyl acetate system, and in five binary subsystems
• Henry s law constants of 1-butene, 2-methylpropene, trans-2-butene, and 1,3-butadiene in methanol at 374 490K
• Vapor pressure measurement for binary and ternary systems containing a phosphoric ionic liquid
• Liquid liquid equilibria of aqueous mixtures containing selected dibasic esters and/or methanol
• Activity coefficients of the species in the methanol solutions of acetaminophen and two silylated derivatives at 298.15K
• Isobaric vapor liquid equilibria for acetone + methanol + lithium nitrate at 100 kPa
• Isochoric heat capacity measurements for H2O+CH3OH mixture in the near-critical and supercritical regions
• Measurement and correlation of vapor liquid equilibria for methanol + methyl laurate and methanol + methyl myristate systems near critical temperature of methanol
• Isobaric vapor liquid equilibria of 1,1-dimethylethoxy-butane + methanol or ethanol +water at 101.32 kPa
• Vapour liquid equilibrium for the systems butane + methanol, +2-propanol, +1-butanol, +2-butanol, +2-methyl-2-propanol at 364.5K
• Vapor pressure measurement for water, methanol, ethanol, and their binary mixtures in the presence of an ionic liquid 1-ethyl-3-methylimidazolium dimethylphosphate
• Liquid liquid equilibria for binary systems of tert-amyl ethyl ether (TAEE), isopropyl tert-butyl ether (IPTBE) and di-sec-butyl ether (DSBE) with water and for ternary systems with methanol or ethanol
• Volumetric properties of the boldine + alcohol mixtures at atmospheric pressure from 283.15 to 333.15K A new method for the determination of the density of pure boldine
• Solubilities of rutin in eight solvents at T = 283.15, 298.15, 313.15, 323.15, and 333.15K
• Solubility of ammonia in liquid mixtures of (water + methanol)
• Limiting activity coefficients in binary mixtures of 1-alkanols and ethylbenzene
• Thermodynamic properties of mixtures containing alkoxypropanol and n-alkanol
• Solubilities of betulin in chloroform + methanol mixed solvents at T = (278.2, 288.2, 293.2, 298.2, 308.2 and 313.2) K
• Vapour liquid equilibria, azeotropic data, excess enthalpies, activity coefficients at infinite dilution and solid liquid equilibria for binary alcohol ketone systems
• Excess molar enthalpies of ethyl acetoacetate + (methanol, +ethanol, +1-propanol, and +2-propanol) at T = (298.15, 313.15 and 328.15)K and p = (0.1 and 10.0)MPa
• Liquid liquid equilibria for the binary system of di-isopropyl ether (DIPE) +water in between 288.15 and 323.15K and the ternary systems of DIPE +water + C1 C4 alcohols at 298.15K
• A new high-pressure vapour liquid equilibrium apparatus
• Isobaric vapour liquid equilibria of binary 1-propoxy-2-propanol mixtures with water and alcohols at reduced pressure
• Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid N-butyl-4-methylpyridinium tosylate using GLC at T = (328.15, 333.15, 338.15, and 343.15)K
• Solubility of antioxidant 1010 in pure alkanols
• Vapor liquid equilibrium in the n-butane +methanol system, measurement and modeling from 323.2 to 443.2K
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium trifluoromethanesulfonate using GLC
• Phase equilibria of glycerol containing systems and their description with the Cubic-Plus-Association (CPA) Equation of State
• Ultrasonic study on binary mixture containing dimethylformamide and methanol over the entire miscibility range (0less thanxless than1) at temperatures 303 323K
• Measurement and calculation of vapor liquid equilibria for methanol + glycerol and ethanol + glycerol systems at 493 573K
• Activity coefficients at infinite dilution measurements for organic solutes and water in the 1-hexyloxymethyl-3-methyl-imidazolium and 1,3-dihexyloxymethyl-imidazolium bis(trifluoromethylsulfonyl)-imide ionic liquids The cation influence
• Experimental measurements of vapor liquid equilibria at low pressure: Systems containing alcohols, esters and organic acids
• (Liquid + liquid) equilibria of the quaternary sysytem methanol + isooctane + cyclohexane + benzene at T = 303.15 K
• Solubilities of N-[(4-bromo- 3,5 - difluorine) phenyl]-acrylamide in methanol-ethanol solution
• Compact apparatus for rapid measurement of high-pressure phase equilibria of carbon dioxide expanded liquids
• Volumetric properties of ionic liquid 1,3-dimethylimidazolium methyl sulfate + molecular solvents at T = (298.15 - 328.15) K
• Phase behavior of the ternary 1-hexyl-3-methylimidazolium tetrafluoroborate + carbon dioxide + methanol system
• Solubility of CF4 in lower alcohols
• High-pressure phase behavior of ternary systems (carbon dioxide + alkanol + hydrophobic ionic liquid)
• Thermodynamic properties of new heat pump working pairs: 1,3-Dimethylimidazolium dimethylphosphate and water, ethanol and methanol
• Gas-liquid chromatography measurements of activity coefficients at infinite dilution of hydrocarbons and alkanols in 1-alkyl-3-methylimidazolium bis(oxalato)borate
• Volumetric behavior and solution microstructure of methanol-water mixture in sub- and supercritical state via density measurement and MD simulation
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
• Liquid-liquid equilibria for mixtures containing water, methanol, fatty acid methyl esters, and glycerol
• Vapor-liquid and liquid-liquid equilibrium properties of ethane + methanol system at ambient temperature
• Solubility of HFCs in lower alcohols
• Effect of mono-, di- and tri-ethanolammonium tetrafluoroborate protonic ionic liquids on the volatility of water, ethanol, and methanol
• The viscosity of the binary vapor mixture methanol triethylamine at low densities and in the saturated vapor phase of the vapor liquid equilibrium
• Influence of temperature on the (liquid + liquid) equilibria of {methanol + benzene + hexane} ternary system
• Thermophysical properties of pure 1-ethyl-3-methylimidazolium methylsulfate and its binary mixtures with alcohols
• Experimental measurement and modeling of solubility of LiBr and LiNO3 in methanol, ethanol, 1-propanol, 2-propanol and 1-butanol
• Vapor-liquid equilibria of ternary systems with 1-ethyl-3-methylimidazolium ethyl sulfate using headspace gas chromatography
• Liquid-liquid equilibria for systems of water + methanol + methyl anthranilate at several temperatures
• Isothermal vapor-liquid equilibria for methanol and 2,3-dimethyl-2-butene at 343.15 K, 353.15 K, 363.15 K, 373.15 K
• Selection of entrainers for the separation of the binary azeotropic system methanol + dimethyl carbonate by extractive distillation
• A new semi-empirical model for correlating the solubilities of solids in supercritical carbon dioxide with cosolvents
• Solubility of L-phenylalanine in water and different binary mixtures from 288.15 to 318.15 K
• Solid-liquid equilibrium data for the binary system methacrylic acid + methanol in the high methacrylic acid concentration range
• Liquid-liquid equilibria for ternary mixtures of methyl tert-amyl ether + methanol (or ethanol) + imidazolium-based ionic liquids at 298.15 K
• Solubility of itaconic acid in different organic solvents: Experimental measurement and thermodynamic modeling
• Determination of the crystallization thermodynamics and kinetics of L-tryptophan in alcohols - water system
• Ternary liquid-liquid equilibria of bis(trifluoromethylsulfonyl)-amide based ionic liquids + methanol + heptane
• 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
• Phase behavior for carbon dioxide/tetraalkoxysilane systems
• Determination of the solubility, dissolution enthalpy and entropy of 3-pentadecylphenyl acrylate in methanol-ethanol solutions
• Determination of the solubility, dissolution enthalpy and entropy of icariin in water, ethanol, and methanol
• 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 chlocyphos in different solvents
• Determination of the solubility, dissolution enthalpy and entropy of suberic acid in different solvents
• Prediction of different thermodynamic properties for systems of alcohols and sulfate-based anion Ionic Liquids using modified UNIFAC
• A novel static analytical apparatus for phase equilibrium measurements
• Ternary liquid liquid equilibria of trifluorotris(perfluoroethyl)phosphate based ionic liquids + methanol + heptane
• Solubility of puerarin in the binary system of methanol and acetic acid solvent mixtures
• Isobaric vapor liquid equilibrium for binary system of methanol and acetonitrile
• Influence of sulfate-based anion ionic liquids on the separation factor of the binary azeotropic system acetone + methanol
• Liquid liquid equilibria at 298.15 K for ternary mixtures of methyl tert-butyl ether + methanol (or ethanol) + imidazolium-based ionic liquids at atmospheric pressure
• Solubility of succinic acid in different aqueous solvent mixtures: Experimental measurement and thermodynamic modeling
• Investigation on vapor liquid equilibrium for 2-propanol + 1-butanol + 1-pentanol at 101.3 kPa
• Solubility of dimethyl fumarate in water + (methanol, ethanol, 1-propanol) from (278.15 to 333.15) K
• Isobaric vapor-liquid equilibrium data for the binary system methyl acetate + isopropyl acetate and the quaternary system methyl acetate + methanol + isopropanol + isopropyl acetate at 101.3 kPa
• Solubility of propanoic acid 3-(hydroxyphenylphosphinyl)-sodium salts in different solvent
• (Liquid-liquid) equilibria for ternary and quaternary systems of representative compounds of gasoline + methanol at 293.15 K: Experimental data and correlation
• Solubility and pseudopolymorphic transitions in mixed solvent: Meropenem in methanol-water solution
• 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
• Isobaric vapor-liquid equilibrium for methanol + dimethylcarbonate + phosphoric-based ionic liquids
• Using binary mixtures of dicationic ionic liquids for determination ofactivity coefficients at infinite dilution by gas-liquid chromatography
• Measurement and correlation solubility and mixing properties of dimethyl succinylsuccinate in pure and mixture organic solvents from (278.15 to 333.15) K
• Solubilities of crotonic acid in different organic solvents at severaltemperatures from (278.15 to 333.15) K
• Measurement and correlation of the solubility of 4,4'-oxydianiline in different organic solvents
• Solubility of 1, 3, 2-dioxaphosphorinane-5,5-dimethyl -2- (2,4,6-tribromophenoxy)-2-oxide in selected solvents
• Solubility of erythritol in methanol, ethanol and methanol + ethanol: Experimental measurement and thermodynamic modeling
• Isobaric vapor-liquid equilibrium at 101.3 kPa and excess properties at 298.15 K for binary mixtures of methyl phenyl carbonate with methanol or dimethyl carbonate
• Determination and correlation of solubilities of 1,2-bis(2-oxo-5,5-dimethyl-1,3,2-dioxyphosphacyclohexyl-2-imino) ethane in selected solvents
• Vapor-Liquid Equilibrium for Tetrahydrofuran + Methanol + Tetrafluoroborate-based ionic liquids at 101.3 kPa
• Measurements of activity coefficients at infinite dilution in vegetable oils and capric acid using the dilutor technique
• Towards automated characterisation of liquid-liquid equilibria
• The solubility of mercaptosuccinic acid in water + (methanol, ethanol, acetone) mixtures from (278.15 to 333.15 K)
• Solubility of androstenedione in lower alcohols
• Excess molar volumes and excess molar enthalpies in binary systems N-alkyl-triethylammonium bis(trifluoromethylsulfonyl)imide +methanol
• Solid-liquid equilibrium of dicyandiamide in different solvents
• Measurement and correlation of the solubility of maleic anhydride in different organic solvents
• Isobaric vapor-liquid equilibria of the binary mixtures propylene glycol methyl ether + propylene glycol methyl ether acetate, methyl acetate + propylene glycol methyl ether and methanol + propylene glycol methyl ether acetate at 101.3 kPa
• Thermodynamics of fenofibrate and solubility in pure organic solvents
• Thermodynamic models for determination of the solubility of 2, 5-bis(2-furylmethylidene) cyclopentan-1-one in different solvents at temperatures ranging from 308.15 to 403.15 K.
• Measurement and correlation of the solubilities of tetra(5,5-dimethyl-1,3-dioxaphosphorinanyl-2-oxy) neopentane in different pure solvents
• Present status of the modified UNIFAC Model for the prediction of phase equilibria and excess enthalpies for systems with ionic liquids
• 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
• Measurement and correlation for the solubility of dimethyl succinylsuccinate in (methanol + water) and (methanol + dimethyl succinate) binary solvent mixtures
• Thermodynamics of risperidone and solubility in pure organic solvents
• Solid-liquid equilibrium and thermodynamic of 2,5-thiophenedicarboxylic acid in different organic solvents
• Solid-liquid equilibria and the physical properties of binary systems of diphenyl carbonate, dimethyl carbonate, methyl phenyl carbonate, anisole, methanol and phenol
• Experimental and theoretical study of interaction between organic compounds and 1- (4-sulfobutyl)-3-methylimidazolium based ionic liquids
• Solubility of N-Ethylcarbazole in different organic solvent at 279.15 - 319.15 K
• Ternary liquid-liquid equilibria and binary excess and deviation properties at constant temperature for mixtures of dimethyl carbonate, anisole, methanol, phenol and water
• Effect of bivalent cation inorganic salts on isobaric vapor-liquidequilibrium of methyl acetate - methanol system
• Solubility and preferential solvation of sulfadiazine inmethanol + water mixtures at several temperatures
• 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
• Experimental isobaric vapor-liquid equilibrium at atmospheric and sub-atmospheric pressures, excess molar volumes and deviations in molar refractivity from 293.15 K to 318.15 K of diisopropyl ether with methanol and isopropyl alcohol.
• A study on the liquid-liquid equilibrium of 1-alkyl-3-methylimidazolium dialkylphosphate with methanol and dimethyl carbonate
• Separation of acetone and methanol azeotropic system using ionic liquid as entrainer
• Thermodynamic properties of cyclohexane methanol liquid mixture from shear viscosity measurements
• Study of interaction between organic compounds and mono or dicationic oxygenated ionic liquids using gas chromatography
• 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
• Temperature dependent solubility of sodium cyclamate in selected pure solvents and binary methanol + water mixed solvents
• Absorption of CO2 with methanol and ionic liquid mixture at low temperatures
• Thermodynamic analysis for solid liquid equilibrium of mercaptosuccinic acid in a binary solvent of methanol and ethyl acetate at temperatures between (278.15 and 333.15) K
• Measurement, correlation and prediction of isothermal vapor liquid equilibria of different systems containing vegetable oils
• Determination and correlation of solubility and solution thermodynamics of coumarin in different pure solvents
• Solid-liquid equilibrium of diphenyl anilinophosphonate in the different organic solvents
• Separation of methyl acetate + methanol azeotropic mixture using ionic liquids as entrainers
• Excess volumes and excess heat capacities of {1,2- alkanediol + methanol} mixtures and ionic volumes in these systems
• Phase equilibria of (water + propionic acid or butyric acid + 2-methoxy- 2-methylpropane) ternary systems at 298.2 K and 323.2 K
• Measurement and correlation of solubility and dissolution properties of flunixin meglumine in pure and binary solvents
• Measurement of vapor-liquid-liquid phase equilibrium - Equipment and results
• Measurements and correlations of density and viscosity for short chain (C1-C3) n-alcohol - water mixtures in the temperature range from 350.7 K to 476.2 K at pressures up to 40 MPa
• Isobaric (vapor-liquid) equilibria for binary systems of methanol + 1-(methoxymethoxy)- propane and 1-propanol + 1-(methoxymethoxy)-propane at 101.33 kPa
• Isobaric ternary vapour-liquid equilibrium of methanol(1) + diisopropyl ether(2) + isopropyl alcohol(3) along with methanol + isopropyl alcohol binary data at atmospheric and sub-atmospheric pressures
• Determination and prediction of solubilities of active pharmaceutical ingredients in selected organic solvents
• Isobaric vapor-liquid equilibrium for methyl acetate + methanol system containing different ionic liquids at 101.3 kPa
• Experimental isobaric vapor-liquid equilibrium for the binary and ternary systems with methanol, methyl acetate and dimethyl sulfoxide at 101.3 kPa
• Activity coefficients at infinite dilution for different alcohols and ketones in [EMpy][ESO4]: Experimental data and modeling with PC-SAFT
• Phase equilibria of triolein to biodiesel reactor systems
• Experimental vapour - liquid equilibrium data of the quaternary system Methanol (1) + Isopropyl Alcohol (2) + Water (3) + Glycerol (4) along with Isopropyl Alcohol (2) + Glycerol (4) and Isopropyl Alcohol (2) + Water (3) binary data at atmospheric and sub-atmospheric pressures.
• Measurement and correlation of liquid-liquid equilibrium for the ternary system 2,2,3,3,4,4,5,5-octafluoro-1-pentanol + methanol + water at (298.15, 308.15, and 318.15) K
• Thermal properties and solubility of methyl a-D-glucopyranoside in methanol at different temperatures
• Limiting activity coefficient measurements in binary mixtures of dichloromethane and 1-alkanols (C1 - C4)
• Vapor-liquid equilibria of binary and ternary mixtures containing ethyl lactate and effect of ethyl lactate as entrainer
• Measurement of binary diffusion coefficient and solubility estimation for dyes in supercritical carbon dioxide by CIR method
• 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
• Bubble point pressures of binary system of methanol and methyl propionate
• High pressure vapor-liquid equilibria for binary methane and protic ionic liquid based on propionate anions
• Measurement and correlation of isobaric vapor-liquid equilibria of methanol + tetrahydrofuran + 1-alkyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide at 101.3 kPa
• Ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate: An efficient entrainer to separate methanol + dimethyl carbonate azeotropic mixture
• Measurement and correlation of ternary vapor-liquid equilibria for methanol + glycerol + fatty acid methyl ester (methyl laurate, methyl myristate, methyl palmitate) systems at elevated temperatures and pressures
• Liquid-liquid equilibrium in binary and ternary mixtures containing formaldehyde, water, methanol, methylal, and poly(oxymethylene) dimethyl ethers
• Isobaric vapor-liquid equilibrium for methanol + methyl ethyl ketone + bis(trifluoromethylsulfonyl)imide-based ionic liquids at 101.3 kPa
• Determination and correlation of solubility and solution thermodynamics of ethenzamide in different pure solvents
• Measurement and prediction of phase equilibria of ethylene + vinyl acetate + methanol + poly(ethylene-co-vinyl acetate) systems
• Determination and correlation of solubility of linezolid form II in different pure and binary solvents
• Separation of methanol + dimethyl carbonate azeotropic mixture using ionic liquids as entrainers
• Effect of composition and temperature variations on thermophysical properties of binary and ternary mixtures of 1-ethyl-3-methylimidazolium ethylsulfate with 1-butanol and /or methanol
• In situ measurement of liquid-liquid equilibria by medium field nuclear magnetic resonance
• Evaluation of the solvent structural effect upon the vapor-liquid equilibrium of [C4C1im][Cl] + Alcohols
• Isobaric vapor-liquid equilibrium for ternary mixtures of acetone + methanol + ionic liquids at 101.3kPa
• Determination and correlation of solubility of N-methyl-3,4,5- trinitropyrazole (MTNP) in ten pure solvents from 283.15 K to 323.15 K
• Thermodynamic analysis of the solubility of polymorphic cytarabine in a variety of pure solvents
• High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
• Measurement and correlation of density and viscosity of n-alcohol-water mixtures at temperatures up to 618 K and at pressures up to 40 MPa
• Partial molar volume of NaCl and CsCl in mixtures of water and methanol by experiment and molecular simulation
• 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
• Solubility and dissolution characteristics of capecitabine in pure lower alcohols and water with methanol mixture solvents at atmospheric pressure and different temperatures
• Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
• Solubilities of six lithium salts in five non-aqueous solvents and in a few of their binary mixtures
• Ternary liquid-liquid equilibrium of an azeotropic mixture (hexane + methanol) with different imidazolium-based ionic liquids at T = 298.15 K and 101.325 kPa
• 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
• Extractive distillation of methylal/methanol mixture using ethylene glycol as entrainer
• Solubility of carbon dioxide in methanol from 213.15 K to 273.15 K: Measurement and modeling
• Liquid-liquid equilibria of water + solutes (acetic acid/ acetol/furfural/guaiacol/methanol/phenol/propanal) + solvents (isopropyl acetate/toluene) ternary systems for pyrolysis oil fractionation
• 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
• Isobaric vapor-liquid equilibrium for methanol + methyl acetate with ionic liquids [OMMIM][Tf2N] and [OMIM][Tf2N] as entrainers at 101.3 kPa
• Tetramethylammonium chloride + glycerol deep eutectic solvent as separation agent for organic liquid mixtures: Assessment from experimental limiting activity coefficients
• Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-butyl-1-methylpyrrolidinium dicyanamide
• Density, excess molar volume, and COSMO-RS study of reactive aqueous solutions containing formaldehyde
• 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
• Separation of acetonitrile and methanol azeotropic mixture using imidazolium-based ionic liquids as entrainers
• Liquid-liquid equilibria of n-heptane, methanol and deep eutectic solvents composed of carboxylic acid and monocyclic terpenes
• Measurement and correlation of the isobaric vapor-liquid equilibria of methanol + methyl carbonate + Bis(trifluoromethylsulfonyl)imide-based ionic liquidsat 101.3 kPa
• 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
• Experimental measurements and thermodynamic modeling of Coumarin-7 solid solubility in supercritical carbon dioxide: Production of nanoparticles via RESS method
• Measurements of activity coefficients at infinite dilution for organic solutes in two quaternary ammonium-based ionic liquids [DDA][ClO4] and [DDA][BF4]
• Thermodynamic equilibrium of hexamethylenediammonium glutarate in mono-solvents and binary solvent systems
• Measurement and modeling of infinite dilution activity coefficients of organic compounds in an equimolar ionic liquid mixture of [Bmim]Cl and [Bmim][Tf2N]
• Isothermal vapor-liquid equilibria at 383.15-413.15 K for the binary system methanol + dimethyl carbonate and the pressure dependency of the azeotropic point
• Separation abilities of three acetate-based ionic liquids for benzene-methanol mixture through vapor-liquid equilibrium experiment at 101.3 kPa
• Application of trihexyltetradecylphosphonium dicyanamide ionic liquid for various types of separations problems: Activity coefficients at infinite dilution measurements utilizing GLC method
• New vapour-liquid equilibrium data on the ternary system carbon dioxide - methanol - dimethyl sulphoxide
• Solubility measurements and thermodynamic modeling of pyrazinamide in five different solvent-antisolvent mixtures
• Temperature dependence of the volumetric properties of some alkoxypropanols + n-alkanol mixtures
• Liquid--liquid equilibria for mixtures of {methyl acetate + methanol + n-alkane (C10--C12)} at several temperatures and 1 atm
• Excess molar volumes V , isothermal compressibilities k, and thermal expansivities alpha of {(1- x)H2O+xCH3OH} at T =(298.15 to 523.15) K and pressures up to 60 MPa
• Excess molar enthalpies of ternary mixtures of (methanol, ethanol + 2-propanol + 1,4-dioxane) at T ? 298:15 K
• (Liquid + liquid) equilibrium of (dibutyl ether + methanol + water) at different temperatures
• Apparent molar volume and isentropic compressibility of ionic liquid 1-butyl-3-methylimidazolium bromide in water, ethanol, and ethanol at T = (298.15 to 318.15) K
• Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid 1-butyl-3-methyl-imidazolium 2-(2-methoxyethoxy) ethyl sulfate using g.l.c. at T = (298.15, 303.15, and 308.15) K
• (p, q, T) properties, and apparent molar volumes V/ of ZnBr2 in methanol at T = (298.15 to 398.15) K and pressures up to p = 40 MPa
• Vapor pressure of heat transfer fluids of absorption refrigeration machines and heat pumps: Binary solutions of lithium nitrate with methanol
• The (p,q,T) of (methanol + benzene) and (methanol + ethylbenzene)
• Excess enthalpy HE and massic heat capacity cp of (water + methanol) at temperatures between 323 K and 513 K and pressures up to 10 MPa
• Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid hexyl-3-methyl-imidazolium bis(trifluoromethylsulfonyl)-imide using g.l.c. at T = (298.15, 313.15, and 333.15) K
• (Liquid + liquid) equilibria for ternary mixtures of (methanol or ethanol + toluene or m-xylene + n-dodecane)
• 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)
• Tailor-made ionic liquids
• (p, rho , T) properties and apparent molar volumes of CaCl2 in methanol at T=(298.15 to 398.15) K and pressures up to 40 MPa
• Experimental and predicted volumetric and refractive index properties of ternary mixtures of iodoethane with toluene and alcohols at temperature 298.15 K and pressure 101 kPa
• Excess molar volumes and partial molar volumes for (propionitrile + an alkanol) at T = 298.15 K and p = 0.1 MPa
• Investigation of the vapor pressure p of zinc bromide or zinc chloride solutions with methanol by static method
• Measurement of activity coefficients at infinite dilution using polar and non-polar solutes in the ionic liquid 1-methyl-3-octyl-imidazolium diethyleneglycolmonomethylethersulfate at T = (288.15, 298.15, and 313.15) K
• Dynamic viscosities of the ternary liquid mixtures (dimethyl carbonate + methanol + ethanol) and (dimethyl carbonate + methanol + hexane) at several temperatures
• Volumetric and compressibility behaviour of ionic liquid, 1-n-butyl-3-methylimidazolium hexafluorophosphate and tetrabutylammonium hexafluorophosphate in organic solvents at T = 298.15 K
• Henry's law constants and infinite dilution activity coefficients of cis-2-butene, dimethylether, chloroethane, and 1,1-difluoroethane in methanol, 1-propanol, 2-propanol, 1-butanol, 2-butanol, isobutanol, tert-butanol, 1-pentanol, 2-pentanol, 3-pentanol, 2-methyl-1-butanol, 3-methyl-1-butanol, and 2-methyl-2-butanol
• Bubble point temperatures of the binary mixtures of nitrobenzene with C1 C4 aliphatic alcohols at 94.95 kPa
• (p, rho, T) properties and apparent molar volumes V/ of LiNO3 in methanol
• Application of Prigogine Flory Patterson theory to excess molar volume and speed of sound of 1-n-butyl-3-methylimidazolium hexafluorophosphate or 1-n-butyl-3-methylimidazolium tetrafluoroborate in methanol and acetonitrile
• (Vapor + liquid) equilibria of the binary mixtures of m-cresol with C1 C4 aliphatic alcohols at 95.5 kPa
• Densities, viscosities, and ultrasonic velocity studies of binary mixtures of trichloromethane with methanol, ethanol, propan-1-ol, and butan-1-ol at T=(298.15 and 308.15) K
• Study of activity coefficients for sodium iodide in (methanol + benzene) system by (vapour + liquid) equilibrium measurements
• Molar excess enthalpies of binary mixtures of [tributyl phosphate + {CH3(CH2)nOH (n = 0 to 3)}] at 298.15 K
• Excess molar volumes of binary mixtures of 1,3-dimethylimidazolidin-2-one with an alkan-1-ol at the temperatures 283.15 K, 298.15 K, and 313.15 K
• Densities and viscosities of binary mixtures of {dimethylsulfoxide + aliphatic lower alkanols (C1 C3)} at temperatures from T = 303.15 K to T = 323.15 K
• Isobaric specific heat capacity of {xCH3OH + (1-x)H2O} with x = (1.0000, 0.7943, 0.4949, 0.2606, 0.1936, 0.1010, and 0.0496) at T = (280, 320, and 360) K in the pressure range from (0.1 to 15) MPa
• Vapour pressure measurement for binary and ternary systems containing water methanol ethanol and an ionic liquid 1-ethyl-3-ethylimidazolium diethylphosphate
• Measurement of activity coefficients at infinite dilution in 1-hexadecyl-3-methylimidazolium tetrafluoroborate ionic liquid
• Liquid densities and excess molar volumes for (ionic liquids + methanol + water) ternary system at atmospheric pressure and at various temperatures
• Density and speed of sound of lithium bromide with organic solvents: Measurement and correlation
• Density, dynamic viscosity, and derived properties of binary mixtures of methanol or ethanol with water, ethyl acetate, and methyl acetate at T = (293.15, 298.15, and 303.15) K
• Effect of temperature on mixing thermodynamics of a new ionic liquid: {2-Hydroxy ethylammonium formate (2-HEAF) + short hydroxylic solvents}
• Ternary (liquid + liquid) equilibria for mixtures of (methanol + aniline + n-octane or n-dodecane) at T = 298.15 K
• Heat capacities of the mixtures of ionic liquids with methanol at temperatures from 283.15 K to 323.15 K
• Excess volumes of mixing in (N,N-dimethylacetamide + methanol + water) and (N,N-dimethylacetamide + ethanol + water) at the temperature 313.15 K
• Measurement and correlation of solubility of trans-resveratrol in 11 solvents at T = (278.2, 288.2, 298.2, 308.2, and 318.2) K
• Densities, excess volumes, isobaric expansivity, and isothermal compressibility of the (1-ethyl-3-methylimidazolium ethylsulfate + methanol) system at temperatures (283.15 to 333.15) K and pressures from (0.1 to 35) MPa
• Measurements of activity coefficients at infinite dilution of aromatic and aliphatic hydrocarbons, alcohols, and water in the new ionic liquid [EMIM][SCN] using GLC
• Volumetric, acoustic, and viscometric studies of molecular interactions in binary mixtures of dipropylene glycol dimethyl ether with 1-alkanols at 298.15 K
• Densities, excess molar volumes, speeds of sound and isothermal compressibilities for {2-(2-hexyloxyethoxy)ethanol + n-alkanol} systems at temperatures between (288.15 and 308.15) K
• Mixing thermodynamic properties of 1-butyl-4-methylpyridinium tetrafluoroborate [b4mpy][BF4] with water and with an alkan-1ol (methanol to pentanol)
• Excess molar volumes and isentropic compressibility of binary systems {trioctylmethylammonium bis(trifluoromethysulfonyl)imide + methanol or ethanol or 1-propanol} at different temperatures
• Apparent molar volumes, expansibilities, and isentropic compressibilities of selected electrolytes in methanol
• High-pressure densities and derived volumetric properties (excess, apparent, and partial molar volumes) of binary mixtures of {methanol (1) + [BMIM][BF4] (2)}
• Thermodynamic properties of mixtures of N-methyl-2-pyrrolidinone and methanol at temperatures between 298.15 K and 343.15 K and pressures up to 60 MPa
• Activity coefficients at infinite dilution of hydrocarbons, alkylbenzenes, and alcohols in the paramagnetic ionic liquid 1-butyl-3-methyl-imidazolium tetrachloridoferrate(III) using gas liquid chromatography
• Boiling temperature measurement for water, methanol, ethanol, and their binary mixtures in the presence of a hydrochloric or acetic salt of mono-, di-, or tri-ethanolamine at 101.3 kPa
• Temperature dependence on mutual solubility of binary (methanol + limonene) mixture and (liquid + liquid) equilibria of ternary (methanol + ethanol + limonene) mixture
• Phase diagrams of (hexane + methanol + 2,2,2-trifluoroethanol) at three temperatures: Measurement and correlation
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid triethylsulphonium bis(trifluoromethylsulfonyl)imide
• Measurements of activity coefficients at infinite dilution of aliphatic and aromatic hydrocarbons, alcohols, thiophene, tetrahydrofuran, MTBE, and water in ionic liquid [BMIM][SCN] using GLC
• Influence of temperature on the (liquid + liquid) equilibria of {3-methyl pentane + cyclopentane + methanol} ternary system at T = (293.15, 297.15, and 299.15) K
• Physical and excess properties of (methyl acetate + methanol + 1-octyl-3-methyl-imidazolium bis(trifluoromethylsulfonyl)imide) and its binary mixtures at T = 298.15 K and atmospheric pressure
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 4-methyl-N-butyl-pyridinium bis(trifluoromethylsulfonyl)-imide
• Molar excess enthalpies at T = 298.15 K for (1-alkanol + dibutylether) systems
• (Vapor + liquid) equilibria of binary mixtures containing light alcohols and ionic liquids
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium trifluoromethanesulfonate using gas liquid chromatography at T = (313.15, 323.15, and 333.15) K
• Activity coefficients at infinite dilution for solutes in the trioctylmethylammonium bis(trifluoromethylsulfonyl)imide ionic liquid using gas liquid chromatography
• Experimental (vapour + liquid) equilibrium data of (methanol + water), (water + glycerol) and (methanol + glycerol) systems at atmospheric and sub-atmospheric pressures
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-octyl-3-methylimidazolium hexafluorophosphate using gas liquid chromatography at T = (313.15, 323.15, and 333.15) K
• Gas liquid chromatography measurements of activity coefficients at infinite dilution of various organic solutes and water in tri-iso-butylmethylphosphonium tosylate ionic liquid
• Volumetric properties, viscosity and refractive index of the protic ionic liquid, pyrrolidinium octanoate, in molecular solvents
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate [EMIM][TCB] using gas liquid chromatography
• Volumetric, ultrasonic speed, and viscometric studies of salbutamol sulphate in aqueous methanol solution at different temperatures
• Apparent molar volumes and compressibilities of alkaline earth metal ions in methanol and dimethylsulfoxide
• Ultrasonic speeds and isentropic compressibilities of {difurylmethane + (C1 C6) n-alkanol} binary mixtures at T = 298.15 K
• Measurements of activity coefficients at infinite dilution of organic solutes and water in 1-propyl-1-methylpiperidinium bis{(trifluoromethyl)sulfonyl}imide ionic liquid using g.l.c.
• Activity coefficients at infinite dilution of organic solutes in N-alkylpyridinium bis(trifluoromethylsulfonyl)imide ([CnPY][NTf2], n = 2, 4, 5) using gas liquid chromatography
• Thermodynamic study of binary mixtures containing 1-butylpyridinium tetrafluoroborate and methanol, or ethanol
• Measurement and correlation of solubilities of apigenin and apigenin 7-O-rhamnosylglucoside in seven solvents at different temperatures
• Phase equilibrium data and thermodynamic modelling of the system (propane + DMF + methanol) at high pressures
• Measurements of activity coefficients at infinite dilution of organic compounds and water in isoquinolinium-based ionic liquid [C8iQuin][NTf2] using GLC
• Vapor pressures, excess enthalpies, and specific heat capacities of the binary working pairs containing the ionic liquid 1-ethyl-3-methylimidazolium dimethylphosphate
• 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
• Application of the ERAS model to volumetric properties of binary mixtures of banana oil with primary and secondary alcohols (C1- C4) at different temperatures
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-butyl-3-methylimidazolium hexafluoroantimonate using gas liquid chromatography at T = (313.15, 323.15, and 333.15) K
• Thermophysical properties of binary mixtures of {ionic liquid 2-hydroxy ethylammonium acetate + (water, methanol, or ethanol)}
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
• Phase behavior of (CO2 + methanol + lauric acid) system
• Volumetric and viscometric properties of binary mixtures of {methyl tert-butyl ether (MTBE) + alcohol} at several temperatures and p = 0.1 MPa: Experimental results and application of the ERAS model
• Investigation of sodium 4-nitrotoluene-2-sulfonate solubility in aqueous organic solutions
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(3-hydroxypropyl)pyridinium bis(trifluoromethylsulfonyl)-amide
• Application of the extended real associated solution (ERAS) theory to excess molar enthalpies of benzaldehyde + 1-alkanols (C1 to C5) at T = 298.15 K
• Volumetric properties and enthalpies of solution of alcohols CkH2k+1OH (k = 1, 2, 6) in 1-methyl-3-alkylimidazolium bis(trifluoromethylsulfonyl)imide {[C1CnIm][NTf2] n = 2, 4, 6, 8, 10} ionic liquids
• Effect of ionic liquid 1-methylimidazolium chloride on the vapour liquid equilibrium of water, methanol, ethanol, and {water + ethanol} mixture
• Thermodynamics and activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tetracyanoborate
• Osmotic and activity coefficients in the binary solutions of 1-butyl-3-methylimidazolium chloride and bromide in methanol or ethanol at T = 298.15 K from isopiestic measurements
• Ebulliometric determination and prediction of (vapor + liquid) equilibria for binary and ternary mixtures containing alcohols (C1 C4) and dimethyl carbonate
• Effect of the temperature on the physical properties of pure 1-propyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide and characterization of its binary mixtures with alcohols
• Interactions of volatile organic compounds with the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
• Volumetric and surface properties of pure ionic liquid n-octyl-pyridinium nitrate and its binary mixture with alcohol
• 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
• Properties of pure 1-methylimidazolium acetate ionic liquid and its binary mixtures with alcohols
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpiperidinium bis(trifluoromethylsulfonyl)-amide
• Surface thermodynamics of binary mixtures of aliphatic alcohols in heavy water
• Thermodynamic properties of binary mixtures combining two pyridinium-based ionic liquids and two alkanols
• Experimental study on the calorimetric data of cyclohexanol with alkanols (C1-C4) and correlation with Wilson, NRTL and UNIQUAC models at 300 K
• 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
• H2 solubility in methanol in the presence of CO2 and O2
• Phase equilibrium measurements and thermodynamic modeling of methane alcohol systems at ambient temperature
• Ternary (liquid + liquid) equilibria for b-citronellol in aqueous alcohol at different temperatures
• Effect of alkanolammonium formates ionic liquids on vapour liquid equilibria of binary systems containing water, methanol, and ethanol
• Measurement of (vapor + liquid) equilibrium for the systems {methanol + dimethyl carbonate} and {methanol + dimethyl carbonate + tetramethylammonium bicarbonate} at p = (34.43, 67.74) kPa
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium trifluorotris(perfluoroethyl)phosphate
• Measurement and correlation of the solubility of 2,3,4,5-tetrabromothiophene in different solvents
• Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds: Saturated fatty acids
• Partial molar volume of tertiary amines in methanol at T = 298.15 K. Solvation, shape and specific interactions
• Measurement and correlation of solubility of Tetracycline hydrochloride in six organic solvents
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpiperidinium trifluorotris(perfluoroethyl)phosphate
• Henry s constants and activity coefficients of some organic solutes in 1-butyl,3-methylimidazolium hydrogen sulfate and in 1-methyl,3-trimethylsilylmethylimidazolium chloride
• Densities, speeds of sound, and refractive indices for binary mixtures of 1-butyl-3-methylimidazolium methyl sulphate ionic liquid with alcohols at T = (298.15, 303.15, 308.15, and 313.15) K
• Interactions of volatile organic compounds with the ionic liquids 1-butyl-1-methylpyrrolidinium tetracyanoborate and 1-butyl-1-methylpyrrolidinium bis(oxalato)borate
• Thermophysical properties of biodiesel and related systems. Part I. Vapour liquid equilibrium at low pressures of binary and ternary systems involving methanol, ethanol, glycerol, water and NaCl
• Physicochemical properties and activity coefficients at infinite dilution for organic solutes and water in a novel bicyclic guanidinium superbase-derived protic ionic liquid
• Experimental measurements and predictions of density, viscosity, and carbon dioxide solubility in methanol, ethanol, and 1-propanol
• Properties of pure n-butylammonium nitrate ionic liquid and its binary mixtures of with alcohols at T = (293.15 to 313.15) K
• Isothermal (vapour + liquid) equilibria for binary mixtures of diisopropyl ether with (methanol, or ethanol, or 1-butanol): Experimental data, correlations, and predictions
• Solubilities of evodiamine in twelve organic solvents from T = (283.2 to 323.2) K
• Volume effects for binary mixtures of propane-1,2-diol with methanol, propan-1-ol, hexan-1-ol, octan-1-ol, or nonan-1-ol at temperatures (293.15 to 318.15) K
• Thermodynamics of 1-alkanol + linear polyether mixtures
• Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds Part II: C18 fatty acids
• Experimental and theoretical study on infinite dilution activity coefficients of various solutes in piperidinium ionic liquids
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpyrrolidinium trifluorotris(perfluoroethyl)phosphate
• Measurements of activity coefficients at infinite dilution for organic solutes and water in N-hexylisoquinolinium thiocyanate, [HiQuin][SCN] using GLC
• Activity coefficients at infinite dilution of organic solutes in N-formylmorpholine and N-methylpyrrolidone from gas-liquid chromatography
• Measurement of critical temperatures and critical pressures for binary mixtures of methyl tert-butyl ether (MTBE) + alcohol and MTBE + alkane
• Probing subsistence of ion-pair and triple-ion of an ionic salt in liquid environments by means of conductometric contrivance
• Quantitative NMR spectroscopy of binary liquid mixtures (aldehyde + alcohol) Part I: Acetaldehyde + (methanol or ethanol or 1-propanol)
• Density and surface tension of pure ionic liquid 1-butyl-3-methylimidazolium L-lactate and its binary mixture with alcohol and water
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-hydroxyethyl)- 3-methylimidazolium trifluorotris(perfluoroethyl)phosphate
• Activity coefficients at infinite dilution of organic solutes in diethylene glycol and triethylene glycol from gas-liquid chromatography
• Excess molar enthalpies of {diethyl oxalate + (methanol, + ethanol, + 1-propanol, and + 2-propanol)} at T = (288.2, 298.2, 313.2, and 328.2) K and p = 101.3 kPa
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid trihexyltetradecylphosphonium bis(trifluoromethylsulfonyl)imide using gas-liquid chromatography at T = (313.15, 333.15, 353.15 and 373.15) K
• Infinite dilution activity coefficients of volatile organic compounds in two ionic liquids composed of the tris(pentafluoroethyl) trifluorophosphate ([FAP]) anion and a functionalized cation
• Quantitative NMR spectroscopy of binary liquid mixtures (aldehyde + alcohol). Part II: (Propanal or butanal or heptanal) + (methanol or ethanol or 1-propanol)
• Thermodynamics of fenoxycarb in solution
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tricyanomethanide
• Effect of tetrabutylammonium bromide on solution behavior of salicylaldehyde anil zinc (II) in methanol at T = (298.15, 308.15 and 318.15) K
• Physical properties of the pure 1-methyl-1-propylpyrrolidinium bis(trifluoromethylsulfonyl)imide ionic liquid and its binary mixtures with alcohols
• Cation effect of ammonium imide based ionic liquids in alcohols extraction from alcohol-alkane azeotropic mixtures
• Thermodynamics and activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylmorpholinium tricyanomethanide
• Partial molar volumes and viscosity B-coefficients for N,N'-ethylenebis(salicylideneiminato)-diaquochromium(III) chloride in methanolic solutions of 1-butyl-2,3-dimethylimidazolium tetrafluoroborate at T = (298.15, 308.15, and 318.15) K
• Measurement of activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium 2-(2-methoxyethoxy) ethylsulfate at T = (308.15, 313.15, 323.15 and 333.15) K using gas + liquid chromatography
• Measurement of activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-hexyl-1,4-diaza[2.2.2]bicyclooctanium bis(trifluoromethylsulfonyl)imide using gas-liquid chromatography
• Activity coefficients at infinite dilution of organic solutes in 1-hexyl-3- methylimidazolium trifluoroacetate and influence of interfacial adsorption using gas liquid chromatography
• Physicochemical properties of two 1-alkyl-1-methylpyrrolidinium bis[(trifluoromethyl)sulfonyl]imide ionic liquids and of binary mixtures of 1-butyl-1-methylpyrrolidinium bis[(trifluoromethyl)sulfonyl]imide with methanol or acetonitrile
• Isobaric (vapor + liquid) equilibrium data for the binary system methanol + 2-butyl alcohol and the quaternary system methyl acetate + methanol + 2-butyl alcohol + 2-butyl acetate at P = 101.33 kPa
• Determination and correlation of the solubility of four Bronsted-acidic ionic liquids based on benzothiazolium cations in six alcohols
• Measurement and correlation of critical properties for binary mixtures and ternary mixtures containing gasoline additives
• Quantitative NMR spectroscopy of binary liquid mixtures (aldehyde + alcohol). Part III: (1-decanal or 3-phenylpropanal or 2-chlorobenzaldehyde) + (methanol or ethanol or 1-propanol)
• Effect of the temperature on the physical properties of the pure ionic liquid 1-ethyl-3-methylimidazolium methylsulfate and characterization of its binary mixtures with alcohols
• Ionic molar volumes in methanol mixtures with acetonitrile, N,N-dimethylformamide and propylene carbonate at T = 298.15 K
• Non-covalent interactions between {N,N'-bis[(2-pyridinyl)methylene]-1,2-benzenediamine]-bis(nitrato)}Cu(II) with pyridoxine hydrochloride in methanol at T = (298.15, 308.15 and 318.15) K
• Measurement, correlation and dissolution thermodynamics of biological active chalcone in organic solvents at different temperatures
• 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
• Thermodynamic study of the surface of liquid mixtures containing pyridinium-based ionic liquids and alkanols
• Determination and correlation of solubility of spironolactone form II in pure solvents and binary solvent mixtures
• Molar heat capacities for {isomer of butanediol + methanol} as function of mixture composition and temperature
• Thermodynamic models for determination of the solubility of dibenzothiophene in (methanol + acetonitrile) binary solvent mixtures
• VLE measurements using a static cell vapor phase manual sampling method accompanied with an empirical data consistency test
• Determination and correlation of solubility of tylosin tartrate in alcohol mixtures
• Measurement and correlation of solubility of 4-chloro-2,5-dimethoxynitrobenzene and 4-chloro-2,5- dimethoxyaniline in methanol, ethanol, xylene and toluene
• Solvation parameter model and thermodynamic parameters in a dicationic ionic liquid based on pyrrolidinium
• Experimental and theoretically study of interaction between organic compounds and tricyanomethanide based ionic liquids
• Measuring the solubility of CO2 and H2S in sulfolane and the density and viscosity of saturated liquid binary mixtures of (sulfolane + CO2) and (sulfolane + H2S)
• Measurements and modeling of LLE and HE for (methanol + 2,4,4-trimethyl-1-pentene), and LLE for (water + methanol + 2,4,4-trimethyl-1-pentene)
• (Solid + liquid) phase diagram for (indomethacin + nicotinamide)- methanol or methanol/ethyl acetate mixture and solubility behavior of 1:1 (indomethacin + nicotinamide) co-crystal at T = (298.15 and 313.15) K
• Thermodynamic models for determination of the solubility of DL-malic acid in methanol plus (acetonitrile, N,N-dimethylformamide, isopropyl alcohol) binary solvent mixtures
• 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
• Mixing thermodynamic properties of ester-containing solutions: A study on the ternary (methyl alkanoate (pentanoate and methanoate) + methanol) and the corresponding binaries. New contributions to the (ester + ester) interactions
• Density, viscosity, and saturated vapor pressure of ethyl trifluoroacetate
• Activity coefficients at infinite dilution of organic solutes in methylphosphonate based ionic liquids using gas-liquid chromatography
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(3-hydroxypropyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
• (Liquid + liquid) extraction of methanol from alkanes using dialkylphosphate-based ionic liquids as solvents
• Solubility of daidzin in different organic solvents and (ethyl alcohol + water) mixed solvents
• Properties of pure 1,1,3,3-tetramethylguanidine imidazole ionic liquid and its binary mixtures with alcohols at T = (293.15 to 313.15) K
• Activity coefficients at infinite dilution for organic solutes and water in 1-ethyl-1-methylpyrrolidinium lactate
• Measurement and correlation of the solubility of genistin in eleven organic solvents from T = (283.2 to 323.2) K
• Activity coefficients at infinite dilution, physicochemical and thermodynamic properties for organic solutes and water in the ionic liquid ethyl-dimethyl-(2-methoxyethyl)ammonium trifluorotris-(perfluoroethyl)phosphate
• Measurement, correlation of the solubility and solution thermodynamics of 2-cyanoguanidine in (methanol + water) binary solvent systems from T = (283.15 to 343.15) K
• Solubility of tridecanedioic acid in pure solvent systems: An experimental and computational study
• Measurement and correlation of the solubility of 3,4-bis(3-nitrofurazan-4-yl)furoxan (DNTF) in different solvents
• Measurements and equation-of-state modelling of thermodynamic properties of binary mixtures of 1-butyl-1-methylpyrrolidinium tetracyanoborate ionic liquid with molecular compounds
• Volumetric properties, viscosities and refractive indices of binary liquid mixtures of tetrafluoroborate-based ionic liquids with methanol at several temperatures
• Solubility measurement and modelling of 1,8-dinitronaphthalene in nine organic solvents from T = (273.15 to 308.15) K and mixing properties of solutions
• Measurements and modeling for the density of 2-methoxy-2,4,4- trimethylpentane, HE for (methanol + 2-methoxy-2,4,4- trimethylpentane), LLE for (water + 2-methoxy-2,4,4-trimethylpentane) and LLE for (water + methanol + 2-methoxy-2,4,4-trimethylpentane)
• Screening of environmental friendly ionic liquid as a solvent for the different types of separations problem: Insight from activity coefficients at infinite dilution measurement using (gas + liquid) chromatography technique
• Experimental determination and correlation of the solubility of 4-hydroxy-2,5-dimethyl-3(2H)-furanone (DMHF) in six different solvents
• Thermodynamic equilibrium of 4-hydroxy-2,5-dimethyl-3(2H)-furanone in different solvent systems
• Solubility and solution thermodynamics of thymol in six pure organic solvents
• Determination and correlation of pyridoxine hydrochloride solubility in different binary mixtures at temperatures from (278.15 to 313.15) K
• Density, viscosity and excess properties in the trihexyltetradecylphosphonium chloride ionic liquid/methanol cosolvent system
• Correlation and thermodynamic analysis of solubility of diphenhydramine hydrochloride in pure and binary solvents
• Speed of sound measurements of liquid C1-C4 alkanols
• 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
• Measurement and correlation of solubility of thiourea in two solvent mixtures from T = (283.15 to 313.15) K
• Thermodynamic models for determination of the solubility of omeprazole in pure and mixture organic solvents from T = (278.15 to 333.15) K
• Determination and correlation of solubility and solution thermodynamics of oxiracetam in three (alcohol + water) binary solvents
• Measurement and correlation of solubility of cefmenoxime hydrochloride in pure solvents and binary solvent mixtures
• 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)
• Solubility of 3-chloro-N-phenylphthalimide in ten organic solvents from T = (288.15 to 323.15) K: Determination and modelling
• Physicochemical properties of binary mixtures of 1,1,3,3-tetramethylguanidine imidazolide ionic liquid with water and alcohols
• A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
• Thermodynamic models for determination of the solubility of 4-(4-aminophenyl)-3-morpholinone in different pure solvents and (1,4-dioxane + ethyl acetate) binary mixtures with temperatures from (278.15 to 333.15) K
• Solubility measurement and thermodynamic functions of dehydroepiandrosterone acetate in different solvents at evaluated temperatures
• Solution thermodynamics and preferential solvation of sulfamethazine in (methanol + water) mixtures
• Experimental measurement and correlation of the solubility of aloe-emodin in seven pure solvents
• Thermodynamic properties of a CO2-rich mixture (CO2 + CH3OH) in conditions of interest for carbon dioxide capture and storage technology and other applications
• 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
• Measurement and correlation of solubility of pronamide in five organic solvents at (278.15-323.15) K
• Measurement and thermodynamic functions of solid-liquid phase equilibrium of D-(-)-quinic acid in H2O, methanol, ethanol and (H2O + methanol), (H2O + ethanol) binary solvent mixtures
• Equilibrium solubility of sodium 2,4-diaminobenzene sulfonate in liquid mixtures (methanol + water, isopropanol + water, and 1,2-propanediol + water) from 273.15 K to 323.15 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
• Measurement and correlation of the vapor-liquid equilibrium for methanol + acetonitrile + imidazolium-based ionic liquids at 101.3 kPa
• Solubility and solution thermodynamics of 2-methyl-6-nitroaniline in ten organic solvents at elevated temperatures
• Effect of temperature and composition on the surface tension and surface properties of binary mixtures containing DMSO and short chain alcohols
• (Liquid + liquid) equilibria of four alcohol-water systems containing 1,8-cineole at T = 298.15 K
• Solubility determination and thermodynamic models for dehydroepiandrosterone acetate in mixed solvents of (ethyl acetate + methanol), (ethyl acetate + ethanol) and (ethyl acetate + isopropanol)
• 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
• 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
• Measurements and correlations of density, viscosity, and vapour-liquid equilibrium for fluoro alcohols
• Determination and correlation of solubility and thermodynamics of mixing of 4-aminobutyric acid in mono-solvents and binary solvent mixtures
• Separation of aliphatic from aromatic hydrocarbons and sulphur compounds from fuel based on measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid N,N-diethyl-N-methyl-N-(2-methoxy-ethyl)ammonium bis(trifluoromethylsulfonyl)imide
• Solubility determination and thermodynamic modeling of 3-methyl-4- nitrobenzoic acid in twelve organic solvents from T = (283.15-318.15) K and mixing properties of solutions
• Determination and correlation thermodynamic models for solid liquid equilibrium of the Nifedipine in pure and mixture organic solvents
• The standard molar enthalpy of the base catalysed hydrolysis of methyl paraben revisited
• Measurement and modelling of econazole nitrate in twelve pure organic solvents at temperatures from 278.15 K to 318.15 K
• Measurement and prediction of dabigatran etexilate mesylate Form II solubility in mono-solvents and mixed solvents
• Solubility of cefoxitin acid in different solvent systems
• Experimental study on the calorimetric data of 2-butoxyethanol with aliphatic alcohols (C1-C4) and correlation with the Wilson, NRTL and UNIQUAC models at T = 298 K
• Solubility determination and thermodynamic modelling of 2,4-dihydro-5-methyl-2-(4-methylphenyl)-3H-pyrazol-3-one in twelve organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
• Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
• Solubility 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
• Determination and thermodynamic modelling for 4-nitropyrazole solubility in (methanol + water), (ethanol + water) and (acetonitrile + water) binary solvent mixtures from T = (278.15 to 318.15) K
• Correlation and thermodynamic analysis of solubility of cefmetazole acid in three (alcohol + water) binary solvents at temperatures from 278.15 K to 303.15 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
• Thermodynamic and spectroscopic properties of binary mixtures of n-butylammonium butanoate ionic liquid with alcohols at T = (293.15-313.15) K
• Solubility of oxcarbazepine in eight solvents within the temperature range T = (288.15 308.15) K
• Thermodynamic modelling for solubility of 4-nitrobenzaldehyde in different solvents at temperature range from (273.15 to 313.15) K and mixing properties of solutions
• Determination and modelling of troxerutin solubility in eleven mono-solvents and (1,4-dioxane + 2-propanol) binary solvents at temperatures from 288.15 K to 323.15 K
• Fully automatized apparatus for determining speed of sound for liquids in the temperature and pressure interval (283.15-343.15) K and (0.1-95) MPa
• Solubility determination and thermodynamic modelling of 3-amino-1,2,4-triazole in ten organic solvents from T = 283.15 K to T = 318.15 K and mixing properties of solutions
• Investigation on molecular interactions of antibiotics in alcohols using volumetric and acoustic studies at different temperatures
• Thermodynamic modelling for solubility of 5-chloro-1-methyl-4-nitroimidazole in eleven organic solvents from T = (283.15 to 318.15) K
• Thermodynamic properties of L-Theanine in different solvents
• Solubility determination and correlation for o-phenylenediamine in (methanol, ethanol, acetonitrile and water) and their binary solvents from T = (283.15-318.15) K
• Solubility of 3-methyl-4-nitrobenzoic acid in binary solvent mixtures of {(1,4-dioxane, N-methyl-2-pyrrolidone, N,N-dimethylformamide) + methanol} from T = (283.15 to 318.15) K: Experimental determination and thermodynamic modelling
• 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
• Solid-liquid phase equilibrium and dissolution properties of ethyl vanillin in pure solvents
• Solubility of carbon monoxide in bio-oil compounds
• Solubility and solution thermodynamics of 2-methyl-4-nitroaniline in eleven organic solvents at elevated temperatures
• Solubility measurement and thermodynamic functions of 3-nitrobenzaldehyde in different solvents at elevated temperatures
• Determination and thermodynamic modelling for 2-methyl-6-nitroaniline solubility in binary solvent mixtures of ethyl acetate + (methanol, ethanol, n-propanol and isopropanol)
• Determination and correlation of solubility of 11alpha,17alpha-dihydroxy-4-pregnene-3,20-dione in different solvents
• Effect of beta-alanine and the solvent composition on the solubility of solvate of calcium D-pantothenate containing four molecules of methanol and one molecule of water (D-PC*4MeOH*1H2O)
• 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 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
• Excess molar enthalpies of ethane-1,2-diamine plus primary and secondary alkanols (C1-C4) and correlation with Redlich-Kister, Wilson, NRTL and UNIQUAC models at T = 298 K
• Solubility and preferential solvation of some n-alkyl-parabens in methanol + water mixtures at 298.15 K
• Solubility of 2-nitro-p-phenylenediamine in nine pure solvents and mixture of (methanol + N-methyl-2-pyrrolidone) from T = (283.15 to 318.15) K: Determination and modelling
• Effect of temperature on density, sound velocity, and their derived properties for the binary systems glycerol with water or alcohols
• Solubility of 4-methyl-2-nitroaniline in fourteen organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
• Solubility determination and thermodynamic modelling of 3,5-dimethylpyrazole in nine organic solvents from T = (283.15 to 313.15) K and mixing properties of solutions
• Thermodynamic functions for solubility of 3-nitro-o-toluic acid in nine organic solvents from T = (283.15 to 318.15) K and apparent thermodynamic properties of solutions
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
• Solubility and preferential solvation of econazole nitrate in binary solvent mixtures of methanol, ethanol and 1,4-dioxane in water
• Thermodynamic study of solubility for pyrazinamide in ten solvents from T = (283.15 to 323.15) K
• Measurement and correlation of solubility of boscalid with thermodynamic analysis in pure and binary solvents from 288.15 K to 313.15 K
• Solubility modelling and dissolution properties of 5-phenyltetrazole in thirteen mono-solvents and liquid mixtures of (methanol + ethyl acetate) at elevated temperatures
• Solubility, solution thermodynamics and preferential solvation for 4- bromopyrazole in mixed solvents of (methanol/ethanol + water) from T = (283.15 to 318.15) K
• Thermodynamic functions for solubility of 2-mercaptobenzothiazole in eleven pure organic solvents at temperatures from 273.15 K to 318.15 K and mixing properties of solutions
• Solubility modelling, solution thermodynamics and preferential solvation for nitroxoline in solvent mixtures of ethyl acetate + (methanol, ethanol, n-propanol and isopropanol)
• Thermodynamic and molecular investigation into the solubility, stability and self-assembly of gabapentin anhydrate and hydrate
• Solubility and preferential solvation of 2-methyl-4-nitroaniline in mixed solvents of ethyl acetate + (methanol, ethanol, n-propanol and isopropanol)
• Thermodynamics and activity coefficients at infinite dilution for organic compounds and water in the ionic liquid 1-butyl-3-methylimidazolium perchlorate
• Conformational analysis of branched alkanes using limiting partial molar volumes
• Thermodynamic modelling of solubility and preferential solvation for ribavirin (II) in co-solvent mixtures of (methanol, n-propanol, acetonitrile or 1,4-dioxane) + water
• Investigation of surface tension and viscosity for aqueous solutions of MEA-MeOH and DEA-MeOH
• 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
• Thermophysical properties of binary mixtures of 1-butyl-1-methylpyrrolidinium trifluoromethanesulfonate ionic liquid with alcohols at several temperatures
• Separation of binary mixtures based on gamma infinity data using [OMMIM][NTf2] ionic liquid and modelling of thermodynamic functions
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid trihexyl-tetradecyl-phosphonium tricyanomethanide
• Equilibrium solubility, dissolution thermodynamics and preferential solvation of 6-methyl-2-thiouracil in aqueous co-solvent mixtures of methanol, N-methyl-2-pyrrolidone, N,N-dimethyl formamide and dimethylsulfoxide
• Solubility and thermodynamics of vitamin C in binary liquid mixtures involving water, methanol, ethanol and isopropanol at different temperatures
• Ternary liquid-liquid equilibria for systems containing (dimethyl carbonate or methyl acetate + methanol + 1-methylmidazole hydrogen sulfate) at 298.15 K and 318.15 K
• Thermodynamic study of molecular interaction-selectivity in separation processes based on limiting activity coefficients
• Densities and volumetric properties of (choline chloride+urea) deep eutectic solvent and methanol mixtures in the temperature range of 293.15-323.15 K
• Solubility of l-tyrosine in aqueous solutions of methanol, ethanol, n-propanol and dimethyl sulfoxide: Experimental determination and preferential solvation analysis
• Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in ionic liquid [HMMIM][BF4]
• Electrostriction of water and lower alcohols around ammonium nitrate - Volumetric approach
• Thermodynamic behaviour of alkyl lactate-alkanol systems
• The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
• Solubility modelling, solvent effect and preferential solvation of 6-chloropurine in several aqueous co-solvent mixtures between 283.15 K and 328.15 K
• Solubility modelling, solvent effect and preferential solvation of carbendazim in aqueous co-solvent mixtures of N,N-dimethylformamide, methanol, ethanol and n-propanol
• Experimental solubility evaluation and thermodynamic analysis of biologically active D-tryptophan in aqueous mixtures of N,N-dimethylformamide and several alcohols
• 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
• Equilibrium solubility, solvent effect and preferential solvation of chlorhexidine in aqueous co-solvent solutions of (methanol, ethanol, N,N-dimethylformamide and 1,4-dioxane)
• Determination of the thermodynamic parameters of ionic liquid 1-propyl-3-methylimidazolium bromide by gas-liquid chromatography
• The dissolution behavior and apparent thermodynamic analysis of temozolomide in pure and mixed solvents
• Mass density, sound velocity, mixing enthalpy, 1H NMR, Ab initio calculations and intermolecular interactions in binary mixtures of N-methylimidazole + water, +methanol, +ethanol, +1-propanol, +2-propanol
• Liquid-liquid equilibria for azeotropic mixture of methyl tert-butyl ether and methanol with ionic liquids at different temperatures
• Solubility parameter of lenalidomide for predicting the type of solubility profile and application of thermodynamic model
• Solubility modelling and thermodynamic aspect of 2,3-dihydro-6-propyl-2-thioxo-4(1H)-pyrimidinone in binary aqueous solutions of several alcohols
• Effect of 1-ethyl-3-methylimidazolium tetrafluoroborate on the phase equilibria for systems containing 5-hydroxymethylfurfural, water, organic solvent in the absence and presence of sodium chloride
• Experimental determination of vapor liquid equilibrium for methanol + methyl propionate + 1-butyl-3-methylimidazo-lium bis(trifluoromethylsulfonyl)imide at atmospheric pressure
• Equilibrium solubility of dinitolmide in several neat solvents and binary aqueous co-solvent mixtures: Experimental determination and thermodynamic analysis
• Measurement and correlation of solubility of methyleneaminoacetonitrile in pure and binary solvents and thermodynamic properties of solution
• Research on the application of 7-chloro-quinaldine adducts in 7-chloro-quinaldine separation process
• Determination and correlation of solubility and solution thermodynamics of saccharin in different pure solvents
• Thermodynamic and spectroscopic study of binary mixtures containing {dimethyl carbonate (DMC) + alcohols} at T = (288.15-308.15) K and p = (0.1-40) MPa: Experimental study and modelling
• Research and comparison of solid-liquid phase equilibrium and ternary phase diagrams of 1-(3-nitrophenyl)ethanone + 1-(4-nitrophenyl)ethanone in different solvents
• Determination and correlation of solubility and solution thermodynamics of musk xylene in different pure solvents
• Densities and viscosities of binary mixtures of 2,2-diethyl-1,1,3,3-tetramethylguanidinium bis(trifluoromethylsulfonyl)imide with methanol and ethanol
• Solubility of CO2 in methanol, ethanol, 1,2-propanediol and glycerol from 283.15 K to 373.15 K and up to 6.0 MPa
• Experimental isobaric vapour-liquid equilibrium data for the binary system (N, N-dimethyl acetamide + dimethyl sulfoxide) and the quaternary system (sec-butyl acetate + sec-butyl alcohol + N, N-dimethyl acetamide + dimethyl sulfoxide) at 101.3 kPa
• Separation of (water/butan-1-ol) binary systems based on activity coefficients at infinite dilution with phosphonium ionic liquid
• Synergistic effect of salts and methanol in thermodynamic inhibition of sII gas hydrates
• The molar surface quasi-Gibbs energy and its application to the binary mixtures of 1-(2-methoxyethyl)-3-methylimidazolium bis[(trifluoromethyl)sulfonyl]imide [MOEMIM][NTf2] with methanol and ethanol
• 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
• Liquid-liquid extraction of methanol from its mixtures with hexane using three imidazolium-based ionic liquids
• Improving the solubility of temozolomide by cosolvent and its correlation with the Jouyban-Acree and CNIBS/R-K models
• Solubility and mixing thermodynamic properties of levamisole hydrochloride in twelve pure solvents at various temperatures
• Vapor-liquid equilibrium and excess properties of the binary mixtures formed by ethyl isobutyrate and n-alkanols
• Excess molar enthalpies of methyl isobutyl ketone (MIBK) with alkan-1-ols (C1-C6) and their correlations at 298.15 K
• Volumetric properties of the monoethanolamine methanol mixture at atmospheric pressure from 283.15 to 353.15K
• Solubility of hydrogen in methanol at temperatures from 248.41 to 308.20K
• Molar excess enthalpies of ethyl acetate + alkanols at T=298.15K, p=10MPa
• PHYSICAL AND EXCESS PROPERTIES OF BINARY AND TERNARY MIXTURES OF 1,1-DIMETHYLETHOXY-BUTANE, METHANOL, ETHANOL AND WATER AT 298.15K.
• Thermochemistry of adducts of some bivalent transition metal bromides with triphenylphosphine
• Construction of solid liquid phase diagrams in ternary systems by titration calorimetry
• Excess molar enthalpies and heat capacities of dimethyl sulfoxide + seven normal alkanols at 303.15K and atmospheric pressure
• Thermodynamic properties of binary mixtures of 2.2.2-Trifluoroethanol with Water or Alkanols at T=298.15 K
• Excess molar enthalpies for binary mixtures of trimethyl phosphate with alkanols {CH3(CH2)nOH, n = 0 3} at 298.15K
• High-pressure densities and derived volumetric properties (excess and partial molar volumes, vapor-pressures) of binary methanol + ethanol mixtures
• DSC determination of partial ternary phase diagrams of methanol/sodium chloride/water and propylene glycol/sodium chloride/water and their applications for synthesized diagrams
• Excess molar volumes of Diisopropylamine + (C1-C5) Alkan-1-ols: application of the ERAS model and cubic EOS
• Densities and Excess Molar Volumes for Binary Mixtures of Diethanolamine with Water, Methanol, Ethanol and Ternary Solutions of Diethanolamine + Water with Methanol, Ethanol at Atmospheric Pressure from 278.15 to 353.15 K
• Solubilities of succinimide in different pure solvents and binary methanol+ethyl acetate solvent mixtures
• Measurement and Correlation for Solubility of Dexibuprofen in Different Solvents from (263.15 to 293.15) K
• Solubilities of 1,3-dimethyl-1,1,3,3-tetraphenyldisiloxane in different solvents from (288.15 to 313.15) K
• Solubility in binary solvent mixtures: pyrene dissolved in alcohol + toluene mixtures
• Measurement of thermal conductivities of [mmim]DMP/CH3OH and [mmim]DMP/H2O by freestanding sensor-based 3w technique
• Probing molecular interactions of ionic liquid in industrially important solvents by means of conductometric and spectroscopic approach
• Solubility of disodium cytidine 5'-monophosphate in different binarymixtures from 288.15 K to 313.15 K
• Refractive properties of binary mixtures containing pyridinium-basedionic liquids and alkanols
• Effects of temperature and concentration on interactions in (methanol + ethyl acetate) and (ethanol + methyl acetate or ethyl acetate) systems: insights from apparent molar volume and apparent molar isentropic compressibility study
• THERMODYNAMICS OF MIXTURES CONTAINING AMINES. XIV. CpEm OF BENZYLAMINE WITH HEPTANE AT 293.15 K OR WITH METHANOL, 1-PROPANOL OR 1-PENTANOL AT (293.15-308.15) K
• Study of intermolecular interactions in binary mixtures of 2-(dimethylamino)ethanol with methanol and ethanol at various temperatures
• Measurement and correlation of the solubility of (1-benzyl-1H-1,2,3-triazole-4-yl)methanol in water and alcohols at temperatures from 292.15 K to 310.15 K
• Vapor-liquid equilibria, density and sound velocity measurements of (water or methanol or ethanol + 1,3-propanediol) binary systems at different temperatures
• Low cost apparatus for rapid boiling point determination of small air sensitive samples under inert atmosphere
• Renewable platform chemicals: Thermochemical study of levulinic acid esters
• Measurement and correlation of solubility of carbendazim in lower alcohols
• A new analysis method for improving collection of vapor-liquid equilibrium (VLE) data of binary mixtures using differential scanning calorimetry (DSC)
• Experimental solubility and thermodynamic aspects of methylene blue in different solvents
• Apparent thermodynamic analysis and the dissolution behavior of levamisole hydrochloride in three binary solvent mixtures
• 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
• Modified Method for Measuring the Solubility of Pharmaceutical Compounds in Organic Solvents by Visual Camera
• Experimental and Computational Thermodynamic Properties of (Benzyl alcohol + Alkanols) Mixtures
• Solubility and Saturation Apparent Volume of Propranolol Hydrochloride in Some Binary Aqueous Cosolvent Mixtures at 298.15 K
• Solubility and Solution Thermodynamics of Gibberellin A4 in Different Organic Solvents from 278.15 K to 333.15 K
• Lamotrigine Solubility in Some Nonaqueous Solvent Mixtures at 298.2 K
• Density and Viscosity for Binary Mixtures of the Ionic Liquid 2,2-Diethyl-1,1,3,3-Tetramethylguanidinium Ethyl Sulfate with Water, Methanol, or Ethanol
• Density and Excess Molar Volumes of 1-Butanol + Methanol + Electrolyte Systems in the Temperature Range (293.15 308.15) K
• Solubility Measurement and Correlation for 2- Naphthaldehyde in Pure Organic Solvents and Methanol + Ethanol Mixtures
• Investigation of Surface and Solubility Properties of N-Vinylimidazolium Tetrahalogenidoferrate(III) Magnetic Ionic Liquids Using Density Functional Theory
• Solubilities of 3-Chlorophthalic Anhydride and 4-Chlorophthalic Anhydride in Different Pure Solvents
• Tie-Line Data for Aqueous Mixtures of Butyric Acid with Diisopropyl Ether at Various Temperatures
• Isobaric Vapor - Liquid Equilibrium for Ethyl acetate + Methanol + Ionic Liquids Ternary systems at 101.3 kPa
• Measurement and Correlation of the Solubility of Maltitol in Different Pure Solvents, Methanol Water Mixtures, and Ethanol Water Mixtures
• Determination and Modeling of MgCl2 Solubility in Methanol, Ethanol, 2-Propanol and Their Mixtures from 283 to 343 K
• Measurement and Correlation of the Solubility of Sodium 2- Chlorotoluene-4-sulfonate in Selected Pure Solvents and Aqueous Organic Solutions
• Solubility Measurement and Simulation of Rivaroxaban (Form I) in Solvent Mixtures from 273.15 to 323.15 K
• Exploration of Solvation Consequence of Ionic Liquid [Bu4PCH3SO3] in Various Solvent Systems by Conductance and FTIR Study
• Solubility Measurement and Modeling of 4,4'-Dihydroxydiphenyl Sulfone in Nine Organic Solvents from T = (278.15 to 313.15) K and Thermodynamic Property of Dissolution
• Solubility of (S)-3-(Aminomethyl)-5-Methylhexanoic Acid in Pure and Binary Solvent Mixtures
• Solubility of Benzoic Acid and Aspirin in Pure Solvents Using Focused Beam Reflective Measurement
• Thermodynamic Models for Determination of the Solubility of Boc-(R)-3-Amino-4-(2, 4, 5-trifluorophenyl)butanoic acid in Different Pure Solvents and (Tetrahydrofuran + n-Butanol) Binary Mixtures with Temperatures from 280.15 to 330.15 K
• Isothermal Vapor Liquid Equilibrium Data for the Methanol + Benzene + Tetraphenylphosphonium Chloride System
• Experimental Measurement and Modeling of the Solubility of Methane in Methanol and Ethanol
• Vapor Liquid Equilibria Measurement of (Methanol + Ethanenitrile + Bis(trifluoromethylsulfonyl) Imide)-Based Ionic Liquids at 101.3 kPa
• Liquid-Liquid Equilibria for Ternary Systems of Water + Methoxycyclopentane (CPME) + Alcohol; Methanol, Ethanol, 1-Propanol, or 2-Propanol
• Solid Liquid Phase Equilibrium of trans-Cinnamic Acid in Several Alcohols: Measurements and Thermodynamic Modeling
• Measurement and Correlation of the Solubility of Antioxidant 626 in Alcohols
• Measurement and Correlation of Solubility of -Aminobutyric Acid in Different Binary Solvents
• Vapor-Liquid Equilibrium Study of the Gamma- Valerolactone-Water Binary System
• Solubility Measurement and Correlation of (+)-Biotin Intermediate Lactone in Different Organic Solvents from (287.15 to 323.75) K
• Vapor Liquid Equilibrium for Methanol + Methyl Palmitate near the Critical Temperature of Methanol
• Solubility of 1,3,5-Benzenetricarboxylic Acid in Different Solvents
• Thermodynamics of 1,3-dimethylurea in eight alcohols
• Measurements of Infinite Dilution Activity Coefficients of Alkanols in the Ionic Liquid Tributylmethylammonium Methyl Sulfate Using HS-SPME/GC/FID
• Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
• Measurement and Correlation of the Solubility for Camptothecine in Different Organic Solvents
• Density, Speed of Sound, Refractive Index, and Viscosity of the Binary Mixtures of N,N-dimethylacetamide with Methanol and Ethanol
• Thermophysical Characterization of the Mixtures of the Ionic Liquid 1-Ethyl-3-Methylimidazolium Acetate with 1-Propanol or 2-Propanol
• Isobaric Vapor Liquid Equilibrium for Binary Systems of Allyl Alcohol with Water, Methanol, and Ethanol at 101.3 kPa
• Solubility Modeling of 4-(Methylsulfonyl)benzaldehyde in Nine Organic Solvents at Elevated Temperatures
• Sucrose Solubility in Binary Liquid Mixtures Formed by Water Methanol, Water Ethanol, and Methanol Ethanol at 303 and 313 K
• Liquid Liquid Equilibria of Binary and Ternary Systems Methanol/Water + n-Hexane, + n-Octane, + n-Dodecane, and + n-Hexadecane in the Temperature Range between T = 283.15 K and T = 333.15 K
• Solubility of Ethyl p-Aminobenzoate in Six Alcohols within (283.15 to 327.15) K
• Measurement and Thermodynamic Modeling of the Solubility of Lamotrigine, Deferiprone, Cefixime Trihydrate, and Cephalexin Monohydrate in Different Pure Solvents from 283.1 to 323.1 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
• Isothermal Vapor Liquid Equilibrium Data for the Toluene + Methanol + N-Butylpyridinium Bromide System
• Liquid Liquid Equilibria for the Ternary System n-Butyl Acetate + Pyrocatechol + Water at Different Temperatures at 101.3 kPa
• Solubility Measurement and Modeling of Methane in Methanol and Ethanol Aqueous Solutions
• Solubility of 2-Ethylanthraquinone in Binary Mixtures of Oligooxymethylene Dimethyl Ethers with Different Number of CH2O Groups of n = 2, 3, and 4 from 293.15 to 343.15 K
• Solubility of 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
• Phase Equilibria for the Hydroesterification of 10-Undecenoic Acid Methyl Ester
• 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
• Isobaric Vapor Liquid Equilibria for Binary Mixtures of .gamma.-Valerolactone + Methanol, Ethanol, and 2-Propanol
• Measurement and Correlation of Solubility on Reactive Crystallization of Methyl D-(-)-4-Hydroxy-phenylglycinate
• 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 and Modeling of Solid Liquid Equilibrium of para-tert-Butylbenzoic Acid in Acetic Acid/Methanol + Water and Acetic Acid + para-tert-Butyltoluene Binary Systems at Various Temperatures
• Isobaric Vapor Liquid Equilibrium for Two Binary Systems (Methanol + Dibutyl Carbonate) and (n-Butanol + Dibutyl Carbonate) at p = 40.0, 70.0, and 100.0 kPa
• Solubilities of Naringin Dihydrochalcone in Pure Solvents and Mixed Solvents at Different Temperatures
• Solubility of 4-Methylsulfonylacetophenone in Nine Pure Solvents and (Ethyl Acetate + n-Hexane) Binary Solvent Mixtures from 278.15 K to 328.15 K
• Measurement and Correlation of Solubility of Loratadine in Different Pure Solvents and Binary Mixtures
• Measurement and Correlation of Solubility of Amorphous Cefmetazole Sodium in Pure Solvents and Binary Solvent Mixtures
• Measurement and Correlation of the Solubility of e-CL-20 in 12 Organic Solvents at Temperatures Ranging from 278.15 to 318.15 K
• Solubility Measurement and Correlation of Two Erlotinib Hydrochloride Polymorphs in Alcohols and Ketones from 273.15 to 323.15 K
• 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 of Vapor Liquid Equilibrium of Methyl Acetate + Methanol + 1-Alkyl-3-methylimidazolium Dialkylphosphates at 101.3 kPa
• 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
• Measurement and Correlation of Phase Equilibria for Isobutyl Acetate + {Ethanol or Methanol} + Water at 303.15 and 323.15 K
• Measurement and Correlation of the Solubility of 2,6-Dihydroxybenzoic Acid in Alcohols and Binary Solvents
• Measurement and Modeling of Solubility of para-tert-Butylbenzoic Acid in Pure and Mixed 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 Liquid Liquid Equilibrium for Quaternary Systems of Water + Methanol or Ethanol + Ethyl Methyl Carbonate + Heptane at 25 deg C
• Determination and Thermodynamic Modeling of Solid Liquid Phase Equilibrium for Esomeprazole Sodium in Monosolvents and in the (Ethanol + Ethyl Acetate) Binary Solvent Mixtures
• Volumetric Properties of Sodium Lauroylsarcosinate in Aqueous Alcohol Solutions of Methanol, Ethanol, and 1-Propanol
• Isobaric Vapor Liquid Equilibria for Two Binary Systems {Propylene Glycol Methyl Ether Acetate + Methanol} and {Propylene Glycol Methyl Ether Acetate + N,N-Dimethylformamide} at p = 30.0, 50.0, and 70.0 kPa
• Measurement and Correlation of Solubility of Theobromine, Theophylline, and Caffeine in Water and Organic Solvents at Various Temperatures
• Isobaric Vapor Liquid Equilibrium for the Binary Systems Dimethyl Disulfide + C1 C4 n-Alkanol at 40.000 and 101.325 kPa
• Pressurized-Synthetic Methodology for Solubility Determination at Elevated Temperatures with Application to Paracetamol in Pure Solvents
• Vapor Liquid Equilibrium and Excess Enthalpy Data for Systems Containing N,N-Dimethylacetamide
• Phase Behavior Data of (CO2 + Toluene + Phenanthrene) and (CO2 + (Methanol + Phenanthrene) Systems at High Pressure
• Separation Effects of Renewable Solvent Ethyl Lactate on the Vapor Liquid Equilibria of the Methanol + Dimethyl Carbonate Azeotropic System
• Solid Liquid Phase Equilibrium of N,N'-Piperazinebis(neopentylglycol)phosphoramidate in Selected Solvents from T = (293.15 to 333.15) K
• Thermal Diffusivity of Methanol to a Pressure of 5 GPa
• 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
• Solubility Determination and Thermodynamic Modeling of Sodium Thioglycolate in Pure and Binary Solvent Mixtures from T = (293.15 to 333.15) K
• Measurement and Correlation for Solubilities of Adipic Acid, Glutaric Acid, and Succinic Acid in Dimethyl Adipate + Methanol Mixtures
• 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
• Solubility and Thermodynamic Behavior of Syringic Acid in Eight Pure and Water + Methanol Mixed Solvents
• Study on the Solubilities of Mononitro-Substituted Products of Nitration of m-Toluic Acid in Several Solvents at Temperatures between 297.65 and 351.75 K
• 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 the Solubility of Azoxystrobin in Seven Monosolvents and Two Different Binary Mixed Solvents
• Measurement and Correlation of Solubility of Resorcinol Bis(cyclic 2,2-dimethyl-1,3-propanediol phosphate) in Selected Solvents from T = 293.15 to 333.15 K
• Solubility of Etoricoxib in Aqueous Solutions of Glycerin, Methanol, Polyethylene Glycols 200, 400, 600, and Propylene Glycol at 298.2 K
• Solubility and Mixing Thermodynamics Properties of p-Toluenesulfonamide and o-Toluenesulfonamide in Seven Monosolvents at Different Temperatures
• Solubility Modeling and Mixing Properties for Benzoin in Different Monosolvents and Solvent Mixtures at the Temperature Range from 273.15 to 313.15 K
• Experimental Vapor-Liquid Equilibria and Thermodynamic Modeling of the Methanol + n-Heptane and 1-Butanol + Aniline Binary Systems
• The Solid-Liquid Equilibrium and Crystal Habit of l-Carnitine Fumarate
• Determination and Correlation of Dipyridamole p-Toluene Sulfonate Solubility in Seven Alcohol Solvents and Three Binary Solvents
• Measurement and Correlation of the Dissolution Equilibria of o-Iodoaniline and p-Iodoaniline in Pure Solvents
• 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 Determination for Carbamazepine and Saccharin in Methanol/Water Mixed Solvent: Basic Data for Design of Cocrystal Production by Antisolvent Crystallization
• Solubility of 2,5-Furandicarboxylic Acid in Eight Pure Solvents and Two Binary Solvent Systems at 313.15-363.15 K
• Viscometric Studies of Molecular Interactions in Binary Liquid Mixtures of Isomeric Xylenes with Methanol
• Solubility and Preferential Solvation of Carbazochrome in Solvent Mixtures of N,N-Dimethylformamide Plus Methanol/Ethanol/n-Propanol and Dimethyl Sulfoxide Plus Water
• Solution Thermodynamics of Benzotriazole in Different Pure Solvents
• Solubilities of 2,5-Furandicarboxylic Acid in Binary Acetic Acid + Water, Methanol + Water, and Ethanol + Water Solvent Mixtures
• 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
• 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
• Liquid-Liquid Equilibrium for Ternary Systems, Water + 5-Hydroxymethylfurfural + (1-Butanol, Isobutanol, Methyl Isobutyl Ketone), at 313.15, 323.15, and 333.15 K
• Measurement and Correlation of the Solubility of Pyrimethanil in Seven Monosolvents and Two Different Binary Mixed Solvents
• Experimental Determination and Thermodynamic Models for Solid-Liquid Equilibrium of 4-(4-Aminophenoxy)-N-methylpyridine-2-carboxamide in Pure and Binary Solvent Mixtures for T = (278.15-328.15) K
• Solubility Modeling, Solvent Effect, and Preferential Solvation of Thiamphenicol in Cosolvent Mixtures of Methanol, Ethanol, N,N-Dimethylformamide, and 1,4-Dioxane with Water
• Measurement and Modelization of VLE for Butyl Acetate with Methanol, Ethanol, 1-Propanol, and 1-Butanol. Experimental Data at 0.15 MPa
• Solubility Measurement and Modeling of 1-(3-nitrophenyl)Ethanone and 1-(4-nitrophenyl)Ethenone in Nine Pure Organic Solvents from T = (278.15 to 318.15) K and Mixing Properties of Solutions
• Determination of Solubility and Thermodynamic Properties of Benzophenone in Different Pure Solvents
• Solubility and Molecular Interactions of Trimetazidine Hydrochloride in 12 Monosolvents and Solvent Mixtures of Methanol + (Ethanol, N,N-Dimethylformamide or Ethyl Acetate)
• Cosolvency and Mathematical Modeling Analysis of Chloroxine in Some Binary Solvent System
• Research on Dissolution Capability of Several Antofloxacin Salts
• Solubility Measurement and Modeling of 2-Amino-4,6-dichoropyrimidine in Ten Pure Solvents and (Ethyl Acetate + Ethanol) Solvent Mixtures
• Solubility Determination and Correlation for Pyridoxal 5-Phosphate Monohydrate in Different Binary Solvents from 278.15 K to 318.15 K
• 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
• Effect of Ionic Liquids on the Binary Vapor-Liquid Equilibrium of Ethyl Acetate + Methanol System at 101.3 kPa
• 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 for the Binary Systems of 2-Butanol + 2-(Methoxymethoxy)-butane and 1-Butanol + 2-(Methoxymethoxy)-butane at 101.3 kPa
• Solubilities of Organic Semiconductors and Nonsteroidal Anti-inflammatory Drugs in Pure and Mixed Organic Solvents: Measurement and Modeling with Hansen Solubility Parameter
• Liquid-Liquid Equilibria for Ternary Systems of (Ethyl Methyl Carbonate + Methanol or Ethanol + Water) at 293.15, 303.15, and 308.15 K
• Thermodynamic Study of Solubility for Imatinib Mesylate in Nine Monosolvents and Two Binary Solvent Mixtures from 278.15 to 318.15 K
• Solubility Determination and Modeling for 4-Nitrobenzonitrile in Binary Solvent Mixtures of Ethyl Acetate Plus (Methanol, Ethanol, n-Propanol, and Isopropanol)
• Solubility Determination of Nicotinamide and Its Application for the Cocrystallization with Benzoic Acid
• Solubility Measurements at 296 and 310 K and Physicochemical Characterization of Abiraterone and Abiraterone Acetate
• Measurement and Correlation of Solubility of 3-Hydroxy-2-naphthoic Acid in Ten Pure and Binary Mixed Organic Solvents from T = (293.15 to 333.15 K)
• Solubility of Toltrazuril and the Effect of a Cosolvent
• 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
• Measurement and Correlation of Solubility and Thermodynamic Properties of Vinpocetine in Nine Pure Solvents and (Ethanol + Water) Binary Solvent
• Solubility Determination and Correlation of Glibenclamide in 11 Monosolvents and (Acetone + Acetonitrile) Binary Solvents from 283.15 K to 323.15 K
• Solubility Modeling and Solution Thermodynamics of 4-Amino-2,6-Dimethoxypyrimidine in Cosolvent Mixtures of Methanol, Ethanol, Isopropanol, and N,N-Dimethylformamide + Water
• Solubility Measurement and Thermodynamic Properties of Levetiracetam in Pure and Mixed Solvents
• Effects of Aliphatic Alcohols on Solubility, Physicochemical Properties, and Morphology of Calcium Sulfate Dihydrate (Gypsum) in Aqueous Sodium Chloride Solution at 35 deg.C
• Solution Thermodynamic Analysis of p-(Aminomethyl)benzoic Acid in Four Binary Solvents from 288.15 to 328.15 K
• Solid-Liquid Equilibrium of Rebaudioside A in Pure and Binary Mixed Solvents at T = (288.15 to 328.15) K
• Solubility and Data Correlation of Isoniazid in Different Pure and Binary Mixed Solvent Systems from 283.15 K to 323.15 K
• 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
• Determination of Ternary Vapor-Liquid Equilibrium of Dimethyl Oxalate-Methanol-1,2-Butanediol under Atmosphere Pressure
• Solubility Measurement and Thermodynamic Model Correlation and Evaluation of 2-Chloro-5-nitroaniline in 12 Pure Solvents
• Thermodynamic Speed of Sound Data for Liquid and Supercritical Alcohols
• Solubility of N-tert-Butylbenzothiazole-2-sulfenamide in Several Pure and Binary Solvents
• A Volumetric and Viscosity Study for the Binary Mixtures of Ammonium-Based Asymmetrical Gemini Ionic Liquids with Alcohols at T = 293.15-333.15 K
• Density and Derived Properties of Binary Mixtures Containing {2-(Dimethylamino)ethyl Methacrylate + Alcohols} at Temperatures from T = (293.15 to 313.15) K and Pressures of up to 35 MPa
• Solubility Determination and Modeling for Artesunate in Binary Solvent Mixtures of Methanol, Ethanol, Isopropanol, and Propylene Glycol + Water
• Experimental Solubility and Density Functional Theory Studies of Deferasirox in Binary Solvent Mixtures: Performance of Polarizable Continuum Model and Jouyban-Acree Model
• Densities and Viscosities for Aqueous Solutions of Sodium Chlorate and Potassium Chlorate + Methanol from (288.15 to 318.15) K at 0.1 MPa
• Solubility Modeling and Solvent Effect of 2-Amino-6-chloropurine in Twelve Neat Solvents
• Equilibrium Solubility of Biapenem in Different Neat and Binary Solvents: Experimental Determination and Model Correlation
• Measurement and Correlation of the Solubility of Mifepristone in Eight Pure and Water + Methanol Mixed Solvents at Temperatures from 273.15 to 318.15 K
• Effect of Solvent Properties and Composition on the Solubility of Ganciclovir Form I
• Measurement and Modeling of Solid-Liquid Equilibria of l-Glutamic Acid in Pure Solvents and Aqueous Binary Mixtures
• Solubility Determination and Thermodynamic Modeling of Buprofezin in Different Solvents and Mixing Properties of Solutions
• Solubility Modeling and Solvent Effect for Flubendazole in 12 Neat Solvents
• Determination and Modeling of Solubility of 4-Aminobenzamide in Different Pure Solvents
• Binary Solid-Liquid Solubility Determination and Model Correlation of Quizalofop-p-ethyl in Different Pure Solvents
• Measurement and Correlation of the Solubility of Baicalin in Several Mixed Solvents
• Solid-Liquid Equilibrium of Azacyclotridecan-2-one in 15 Pure Solvents from T = 273.15 to 323.15 K: Experimental Determination and Thermodynamic Modeling
• Measurement and Correlation of the Solubility of 2-Cyanoacetamide in 14 Pure Solvents and the Mixing Properties of Solutions
• Solubility Determination of 1,5-Naphthalenediamine and 1,8-Naphthalenediamine in Different Solvents and Mixing Properties of Solutions
• Solubility, Model Correlation, and Solvent Effect of 2-Amino-3-methylbenzoic Acid in 12 Pure Solvents
• Solid-Liquid Equilibria of N-Methylephedrine Enantiomers and Their Mixtures in Two Chiral Ionic Liquids
• Isobaric Vapor-Liquid Equilibrium Measurements and Separation Process for the Quinary Methanol + Methylal + 2-Butanol + 2-(Methoxymethoxy)-butane + (+-)-Di-sec-butoxymethane System
• 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
• Solubility Determination, Modeling, and Preferential Solvation of Terephthalaldehydic Acid Dissolvend in Aqueous Solvent Mixtures of Methanol, Ethanol, Isopropanol, and N-Methyl-2-pyrrolidone
• Equilibrium Solubility, Model Correlation, and Solvent Effect of Indole-3-acetic Acid in Twelve Pure Solvents
• Solubility of l-Phosphinothricin and Its Hydrochloride in Water + (Methanol and Ethanol) Binary Solvent Mixtures from 278.15 to 318.15 K
• 4-Nitrophenzylcyanide Solubility in Several Nonaqueous Solvent Mixtures: Determination and Modeling
• Measurement and Correlation of Solubility of Calcium Formate (Form alpha) in Different Binary Solvent Mixtures at Temperatures from 283.15 to 323.15 K
• Solubility of 4-Chloro-2,5-dimethoxynitrobenzene, 4-Chloro-2,5-dimethoxyaniline, and 2,5-Dimethoxyaniline in Binary and Pure Solvents: Determination and Modeling
• 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
• Isobaric Vapor-Liquid Equilibria of Binary Mixtures of Diethyl Carbonate with Methyl Acetate, n-Propyl Acetate, or Amyl Acetate at 100.17 kPa
• Solubility of Bifonazole in Four Binary Solvent Mixtures: Experimental Measurement and Thermodynamic Modeling
• Thermodynamic Models for Determination of Solid-Liquid Equilibrium of the Buprofezin in Pure and Binary Organic Solvents
• Solubility Determination and Thermodynamic Modeling of 2-Mercaptobenzimidazole in 12 Solvents from T = 278.15 K to T = 318.15 K
• Measurement and Correlation of Solubility of Hydrochlorothiazide in Monosolvents and Binary Solvent Mixtures from 283.15 to 323.15 K
• Solubility Measurement and Thermodynamic Model Correlation of 5-Nitrosalicylaldehyde in Different Solvents
• o-Nitrophenylacetonitrile Solubility in Several Pure Solvents: Measurement, Correlation, and Solvent Effect Analysis
• 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 and Solvent Effect of Acetamiprid in Thirteen Pure Solvents and Aqueous Solutions of Ethanol
• Isobaric Vapor-Liquid Equilibrium for the Binary System of Dimethyl Adipate and 1,6-Hexanediol at 10, 20, and 99 kPa
• Solubility Measurement and Correlation of 2-Oxindole in 12 Pure Organic Solvents
• Determination and Correlation of the Solubility of Musk Ketone in Pure and Binary Solvents at 273.15-313.15 K
• Solubility of d-Aspartic Acid in Several Neat Solvents: Determination, Modeling, and Solvent Effect Analysis
• Effect of Cosolvents on the Solubility of Lenalidomide and Thermodynamic Model Correlation of Data
• 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
• Liquid-Liquid Equilibrium Data for Ternary Systems Containing Alkanes (n-Pentane, n-Hexane, n-Heptane, and n-Octane) + Alcohol (Methanol and Ethanol) + Protic Ionic Liquid (2-HEAF)
• 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
• Electrical Conductivity of Lithium Chloride, Lithium Bromide, and Lithium Iodide Electrolytes in Methanol, Water, and Their Binary Mixtures
• Solubility Determination and Thermodynamic Mixing Properties of 5-Methyl-2-pyrazinecarboxylic Acid in Different Solvents
• Solubility and Thermodynamic Modeling of Sulfanilamide in 12 Mono Solvents and 4 Binary Solvent Mixtures from 278.15 to 318.15 K
• Solubility Determination and Modeling of EGCG Peracetate in 12 Pure Solvents at Temperatures from 278.15 to 318.15 K
• Solubility, Solubility Modeling, and Antisolvent Precipitation of 1,3-Bis(9-carbazolyl)benzene in Organic Solvents
• Solubility Measurement and Thermodynamic Modeling for o-Toluenesulfonamide in 16 Solvents from T = 273.15 to 323.85 K
• Binary Equilibrium Solubility of Amidinothiourea in Monosolvents: Experimental Determination, Model Correlation, and Solvent Effect Analysis
• The Research and Measurement about the Solubility of l-Serine in Eight Common Pure Solvents and Four Binary Mixed Solvents for T = (278.15-333.15) K
• Equilibrium Solubility Determination and Modeling of Fenbendazole in Cosolvent Mixtures at (283.15-328.15) K
• Measurement and Correlation of Solubility of Marbofloxacin in 12 Pure Solvents from 283.15 to 328.15 K
• Measurement and Correlation of the Solubility of Aminocaproic Acid in Some Pure and Binary Solvents
• 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 of Acetoguanamine in Twelve Neat Solvents from 283.15 to 323.15 K
• Solubility and Thermodynamic Modeling of Dimethyl Terephthalate in Pure Solvents and the Evaluation of the Mixing Properties of the Solutions
• Determination and Modeling of d-Histidine Solubility in Several Pure Solvents from 293.15 to 333.15 K
• Solubility Determination of 2-Chloronicotinic Acid and Analysis of Solvent Effect
• Solubility of Carbon Monoxide and Hydrogen in Methanol and Methyl Formate: 298-373 K and 0.3-3.3 MPa
• Solubility measurement and thermodynamic model correlation of sancycline in twelve pure solvents
• Measurement and Correlation of the Solubility of Dienogest in Twelve Pure and Water + Methanol Binary Solvents at Temperatures from 273.15 to 318.15 K
• Solubility and Data Correlation of b-Arbutin in Different Monosolvents from 283.15 to 323.15 K
• Solubility of Phenylphosphinic Acid in Supercritical Carbon Dioxide and the Influence of Methanol on the Solubility Behavior
• Solubility and Solution Thermodynamics of 2,6-Dichloro-4-nitroaniline in 12 Pure Solvents at Temperatures from 278.15 to 323.15 K
• Solubility Behavior and Data Modeling of l-Proline in Different Neat and Binary Solvent Systems
• Thermodynamic Solubility and Mixing Properties of Phenformin in 14 Pure Solvents at Temperatures Ranging from 278.15 to 323.15 K
• Solid-Liquid Phase Equilibrium and Thermodynamic Analysis of N,N'-Diethylthiourea in Different Solvent Systems
• Thermodynamic Solubility of Gatifloxacin in Nonaqueous Solvent Mixtures of N,N-Dimethylformamide Plus Isopropanol/Methanol/n-Propanol/Ethanol
• Infinite Dilution Activity Coefficients in Ethylene Glycol and Ethylene Carbonate
• Isobaric Phase Equilibria of Diethyl Carbonate with Five Alcohols at 101.3 kPa
• Vapor-Liquid Equilibrium Data for Methanol + 1,3-Dioxolane + Water and Constituent Binary Systems at 101.3 kPa.
• Liquid-Liquid Equilibrium and Excess Enthalpies in Binary Systems Methylcyclohexane + Methanol and Methylcyclohexane + N,N-Dimethylformamide
• Solubility of Rofecoxib in the Presence of Methanol, Ethanol, and Sodium Lauryl Sulfate at (298.15, 303.15, and 308.15) K
• Solubility in Binary Solvent Mixtures: Anthracene Dissolved in Alcohol + Acetonitrile Mixtures at 298.2 K
• Ternary Liquid-Liquid Equilibria for Mixtures of 1-Methyl-3-octylimidazolium Chloride + an Alkanol + an Alkane at 298.2 K and 1 bar
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Hexyl-3-methylimidazolium Hexafluorophosphate from Gas-Liquid Chromatography
• Vapor-Liquid Equilibrium for the Carbon Dioxide + Hydrogen + Methanol Ternary System
• Densities, Viscosities, and Surface and Interfacial Tensions of the Ternary Mixture Water + Ethyl Butyrate + Methanol at 303.15 K.
• Determination of Activity Coefficients at Infinite Dilution of Solutes in the Ionic Liquid 1-Hexyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography at the Temperatures 298.15 K and 323.15 K
• Measurement and Correlation of Excess Molar Enthalpies for Ethylene Glycol + Alkanol Systems at the Temperatures (298.15, 308.15, and 323.15) K
• Excess Molar Volumes, Viscosities, and Refractive Indexes for Binary Mixtures of 1-Chlorobutane with Four Alcohols at T = (288.15, 298.15 and 308.15) K
• Solubility of Formaldehyde and Trioxane in Aqueous Solutions
• Liquid-Liquid Equilibria for the Epichlorohydrin + Water + Methanol and Allyl Chloride + Water + Methanol Systems
• High-Pressure Vapor-Liquid Equilibrium Data and Modeling of Propane + Methanol and Propane + Ethanol Systems
• Densities of Water + Diethanolamine + Methanol and Water + N-Methyldiethanolamine + Methanol at Temperatures Ranging from (283.15 to 353.15) K
• Isochoric Heat Capacities of Alkanols and Their Aqueous Mixtures
• Isobaric Vapor Liquid Equilibrium for 2,3-Dimethyl-2-butene + Methanol, + Ethanol, + 2-Propanol, or + 2-Butanol at Atmospheric Pressure
• Vapor Liquid Equilibrium for the Trans-2-Butene + Methanol, + Ethanol, + 2-Propanol, + 2-Butanol and + 2-Methyl-2-Propanol Systems at 332 K
• Critical Properties of Binary and Ternary Mixtures of Hexane + Methanol, Hexane + Carbon Dioxide, Methanol + Carbon Dioxide and Hexane + Carbon Dioxide + Methanol
• Isothermal Vapor Liquid Equilibrium for Binary 2-Methylpropene - C1-C4 Alcohol-Systems
• Determination and Study on the Solubility of Methane in Heptane + Cyclohexane and Heptane + Ethanol at High Pressures
• Dynamic Viscosities of Diethyl Carbonate with Linear and Secondary Alcohols at Several Temperatures
• Vapor-Pressure Measurements of Liquid Solutions at Different Temperatures: Apparatus for Use over an Extended Temperature Range and Some New Data
• Densities and Viscosities of Binary Liquid Mixtures of Trichloroethylene and Tetrachloroethylene with Some Polar and Nonpolar Solvents
• Vapor-Liquid Equilibrium of Durene in Methanol or Ethanol
• Liquid-Liquid Equilibria of Methyl Acetate + Methanol + Octane or Nonane
• Isothermal Vapor-Liquid Equilibrium and Excess Enthalpy Data for the Binary Systems Water + Sulfolane and Methanol + N-Methyl-2-pyrrolidone (NMP)
• Dynamic Viscosities, Densities, and Speed of Sound and Derived Properties of the Binary Systems Acetic Acid with Water, Methanol, Ethanol, Ethyl Acetate and Methyl Acetate at T = (293.15, 298.15, and 303.15) K at Atmospheric Pressure
• Effect of Organic Cosolvents on the Solubility of Ionic Liquids in Supercritical CO2
• Solubility of 11r-Hydroxy-16r,17r-Epoxyprogesterone in Different Solvents between 283 K and 323 K
• Vapor-Liquid Equilibrium and Mixing Properties of Methanol + Diethyl Carbonate and Vinyl Acetate + Diethyl Carbonate Systems
• Measurement and Prediction of Solubility of Four Arylamine Molecules in Benzene, Hexane, and Methanol
• Solid-Liquid Phase Equilibria of Binary and Ternary Mixtures for 2,6-Dimethylnaphthalene and 2,7-Dimethylnaphthalene with Ethanol or Methanol
• Thermodynamic Investigation of Uracil and Its Halo Derivatives. Enthalpies of Solution and Solvation in Methanol
• Isobaric Vapor-Liquid Equilibrium of Acetone + Methanol System in the Presence of Calcium Bromide
• Volumetric Properties of Water + Monoethanolamine + Methanol Mixtures at Atmospheric Pressure from 283.15 to 353.15 K
• Saturation Composition and Density Data for the Sodium Sulfate + Sulfuric Acid + Methanol System
• Measurement of Diffusion Coefficients in Thermodynamically Nonideal Systems
• Vapor-Liquid Equilibrium Behavior of Tolan in Alcohol
• Experimental Investigation of the Influence of NaCl on the Vapor-Liquid Equilibrium of CH3OH + H2O
• Solubility of CO2 in (CH3OH+H2O)
• Dynamic Viscosities of KI or NH4I in Methanol and NH4I in Ethanol at Several Temperatures and 0.1 MPa
• Determination of Activity Coefficients at Infinite Dilution of Polar and Nonpolar Solutes in the Ionic Liquid 1-Ethyl-3-methyl- imidazolium Bis(trifluoromethylsulfonyl) Imidate Using Gas-Liquid Chromatography at the Temperature 303.15 K or 318.15 K
• Mutual Diffusion Coefficients of Some Aqueous Alkanolamines Solutions
• Solubility of Dexamethasone Sodium Phosphate in Different Solvents
• Isobaric Vapor-Liquid Equilibria of Binary Mixtures Containing the Carbonate Group -OCOO-
• Bubble and Dew Point Measurements of the Ternary System Carbon Dioxide + Methanol + Hydrogen at 313.2 K
• Solubilities of Proxetine Hydrochloride Hemihydrate between 286 K and 363 K
• Density, Refractive Index, Speed of Sound, and Vapor-Liquid Equilibria for Binary Mixtures of Methanol + Vinyl Propionate and Vinyl Acetate + Vinyl Propionate. Vapor Pressures of Vinyl Propionate
• Solid - Liquid Phase Equilibrium of Some Aliphatic Alcohols + Cesium Sulfate + Water
• Solubility of NaCl, NaBr, and KCl in Water, Methanol, Ethanol, and Their Mixed Solvents
• Solubility and Density of 2,6-Dimethylnaphthalene in C1-C7 1-Alkanols
• Solubility of 1,3,5-Trioxane in Methanol, Ethanol, and 2-Propanol
• Isothermal and Isobaric Vapor-Liquid Equilibria of the Ternary System of 2,2-Dimethoxypropane + Acetone + Methanol
• Vapor-Liquid Equilibria for the Ternary Systems of Methyl tert-Butyl Ether + Methanol + Methylcyclohexane and Methyl tert-Butyl Ether + Methanol + n-Heptane and Constituent Binary Systems at 313.15 K
• Density, Refractive Index, Speed of Sound at 298.15 K, and Vapor-Liquid Equilibria at 101.3 kPa for Binary Mixtures of Methanol + 2-Methyl-1-butanol and Ethanol + 2-Methyl-1-butanol
• Determination of Activity Coefficients at Infinite Dilution of Solutes in the Ionic Liquid 1-Butyl-3-methylimidazolium Octyl Sulfate Using Gas-Liquid Chromatography at a Temperature of 298.15 K, 313.15 K, or 328.15 K
• Excess Molar Enthalpies of Dimethyl Carbonate and (Methanol, Ethanol, 1-Propanol, and 2-Propanol) at T = (298.15, 313.15, and 328.15) K and p = (0.1, 1.0, and 10.0) MPa
• Density and Viscosity of Binary Mixtures of Ethyl-2-methylbutyrate and Ethyl Hexanoate with Methanol, Ethanol, and 1-Propanol at (293.15, 303.15, and 313.15) K
• Solubility of Cesium Nitrate in Alcohol Aqueous Solutions at (25, 35 and 45 ) C
• Solubility of Lovastatin in Acetone, Methanol, Ethanol, Ethyl Acetate, and Butyl Acetate between 283 K and 323 K
• Solubility of Erythritol in Different Solvents
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 5. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Methyl-3-butyl-imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using Gas-Liquid Chromatography
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 6. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Methyl-3-octyl-imidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Isothermal Vapor-Liquid Equilibrium Data for the System Methanol + Benzene + Sodium Tetraphenylborate
• Volumetric and Speed of Sound of Ionic Liquid, 1-Butyl-3-methylimidazolium Hexafluorophosphate with Acetonitrile and Methanol at T ) (298.15 to 318.15) K
• Experimental and Predicted Results of Anomeric Equilibrium of Glucose in Alcohols
• 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
• Vapor Pressure Measurements of Binary Solutions of CaCl2 with Methanol and Ethanol at T = (298.15 to 323.15) K Using a Static Method
• Mutual Solubilities of Terpene in Methanol and Water and Their Multicomponent Liquid-Liquid Equilibria
• Solubility of Cefazolin Sodium Pentahydrate in Different Solvents between 275 K and 310 K
• Ternary and Quaternary Liquid-Liquid Equilibria of Water + Methanol + Diisopropyl Ether and Water + Methanol + Diisopropyl Ether + Toluene Mixtures
• Solubility of Hydroquinone in Different Solvents from 276.65 K to 345.10 K
• Experimental Measurement and Correlation of Solubility of Pentachloropyridine and Tetrachloropyridine in Methanol, Ethanol, and 2-Propanol
• Measurement and Correlation of Isothermal Vapor-Liquid Equilibrium Data for the System Methanol + Water + Ammonium Bromide
• 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
• High-Pressure Phase Equilibrium for Ethylene + Methanol at 278.15 K and 283.65 K
• Excess Molar Volumes and Viscosities of Binary Mixtures of p-Cresol with Ethylene Glycol and Methanol at Different Temperature and Atmospheric Pressure
• Solubilities of Phenylphosphinic Acid, Hydroxymethylphenylphosphinic Acid, p-Methoxyphenylphosphinic Acid, p-Methoxyphenylhydroxymethylphosphinic Acid, Triphenylphosphine, Tri(p-methoxyphenyl)phosphine, and Tri(p-methoxyphenyl)phosphine Oxide in Selected Solvents
• Vapor Pressures and Activity Coefficients of n-Alcohols and Benzene in Binary Mixtures with 1-Methyl-3-Butyl-Imidazolium Octylsulfate and 1-Methyl-3-Octyl-Imidazolium Tetrafluoroborate
• Isothermal Vapor Liquid Equilibrium for 2-Methylpropene + Methanol, + 1-Propanol, + 2-Propanol, + 2-Butanol, and + 2-Methyl-2-propanol Binary Systems at 364.5 K
• Solubility of Organic Systems Containing 1,4-Dioxan-2-one
• Liquid-Liquid Phase Equilibria of (Ethanol or Methanol + Water) Containing either Dipotassium Hydrogen Phosphate or Sodium Dihydrogen Phosphate
• Densities and Viscosities of Diethyl Carbonate + Toluene, + Methanol, and + 2-Propanol from (293.15 to 363.15) K
• Densities and Viscosities of Binary Mixtures of m-Cresol with Ethylene Glycol or Methanol over Several Temperatures
• Viscosity Measurements on Methanol Vapor and Their Evaluation
• 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
• (p, rho, T) Properties and Apparent Molar Volumes V(phi) of ZnCl2 in CH3OH
• Determination and Study of the Solubility of Methane in Mixtures of Methanol plus Various Hydrocarbons at High Pressures
• Density and Surface Tension of Binary Mixtures of Acetonitrile + 1-Alkanol at 293.15 K
• Solubility of Erythromycin A Dihydrate in Different Pure Solvents and Acetone + Water Binary Mixtures between 293 K and 323 K
• Liquid-Liquid Coexistence Curves for Binary Systems: Methanol + Cyclohexane and + Several Isomers of Hexane
• Activity Coefficients at Infinite Dilution in 1-Alkyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
• Thermodynamic Properties of Mixtures Containing Ionic Liquids: Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Propyl Boronic Acid-3-Alkylimidazolium Bromide and 1-Propenyl-3-alkylimidazolium Bromide Using Inverse Gas Chromatography
• Solubility of o-Phthalic Acid in Methanol + Water and Methanol + Butyl Acetate from (295.87 to 359.75) K
• Densities and Viscosities for the Ternary Systems of Methyl tert-Butyl Ether + Methanol + Benzene and Methyl tert-Butyl Ether + Methanol + Toluene and Their Sub-binary Systems at 298.15 K
• Electrical Conductances of Tetrabutylammonium Bromide, Sodium Tetraphenylborate, and Sodium Bromide in Methanol (1) + Water (2) Mixtures at (298.15, 308.15, and 318.15) K
• Excess Molar Enthalpies of 1,2-Propanediol + Alkan-1-ols (C1-C6) and Their Correlations at 298.15 K and Ambient Pressure (81.5 kPa)
• Compressibility Studies of Binary Solutions Involving Water as a Solute in Nonaqueous Solvents at T ) 298.15 K
• Physical Properties of Binary Mixtures of the Ionic Liquid 1-Methyl-3-octylimidazolium Chloride with Methanol, Ethanol, and 1-Propanol at T = (298.15, 313.15, and 328.15) K and at P ) 0.1 MPa
• Ebulliometric Determination of Vapor-Liquid Equilibria for Methanol + Ethanol + Dimethyl Carbonate
• Measurement and Correlation of Solubilities of Luteolin in Organic Solvents at Different Temperatures
• Solubility and Melting Properties of Salicylic Acid
• Vapor Pressure Measurement and Prediction for Ethanol + Methanol and Ethanol + Water Systems Containing Ionic Liquids
• Vapor-Liquid Equilibrium for Binary Systems of Diacetyl with Methanol and Acetone
• Solubility and Melting Properties of Salicylamide
• Effect of Pressure on the Static Relative Permittivities of Alkan-1-ols at 298.15 K
• Measurement and Modeling of Phase Equilibria for Ethanol + Water + Methanol at Isobaric Condition
• Experimental Study of Thermodynamic Properties of Mixtures Containing Ionic Liquid 1-Ethyl-3-methylimidazolium Ethyl Sulfate Using Gas-Liquid Chromatography and Transpiration Method
• Infinite Dilution Activity Coefficients for Trihexyltetradecyl Phosphonium Ionic Liquids: Measurements and COSMO-RS Prediction
• Solubility of D-(-)-p-Hydroxyphenylglycine Dane Salt in Mixtures of Methanol and Ethanol
• Solubility of D-p-Hydroxyphenylglycine in Water, Methanol, Ethanol, Carbon Tetrachloride, Toluene, and N,N-Dimethylformamide between 278 K and 323 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 Phenazine-1-carboxylic Acid in Water, Methanol, and Ethanol from (278.2 to 328.2) K
• Vapor-Liquid Equilibria and HE for Binary Systems of Dimethyl Ether (DME) with C1-C4 Alkan-1-ols at 323.15 K and Liquid-Liquid Equilibria for Ternary System of DME + Methanol + Water at 313.15 K
• Ternary Isobaric Vapor-Liquid Equilibria of Methanol + N-Methyldiethanolamine + Water and Methanol + 2-Amino-2-methyl-1-propanol + Water Systems
• Volumetric Properties of the Binary Methanol + Chloroform and Ternary Methanol + Chloroform + Benzene Mixtures at (288.15, 293.15, 298.15, 303.15, 308.15, and 313.15) K
• Vapor-Liquid Equilibria Data for Methanol + 2-Propanol+ 2-Methyl-2-butanol and Constituent Binary Systems at 101.3 kPa
• Isobaric Vapor-Liquid Equilibria for Binary and Ternary Mixtures of Methanol, Ethanoic Acid, and Propanoic Acid
• Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Butyl-3-methyl-pyridinium Trifluoromethanesulfonate
• Density and Viscosity of Clopidogrel Hydrogen Sulfate + Methanol and Clopidogrel Hydrogen Sulfate + Ethanol from (278.15 to 313.15) K
• Solubilities of Nizatidine in Water, Methanol, Ethanol, Acetone, and Ethyl Acetate from (273.15 to 343.15) K
• Excess Molar Enthalpies of Benzyl Alcohol + Alkanols (C1-C6) and Their Correlations at 298.15 K and Ambient Pressure
• Excess Molar Volumes of 1,3-Diethyl Propanedioate with Methanol, Ethanol, Propan-1-ol, Propan-2-ol, Butan-2-ol, 2-Methyl-propan-1-ol, and Pentan-1-ol at T = (288.15, 298.15, 313.15, and 328.15) K
• Solubility of Artemisinin in Different Single and Binary Solvent Mixtures Between (284.15 and 323.15) K and NRTL Interaction Parameters
• 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
• 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
• Solubility of Scutellarin in Methanol, Water, Ethanol, and Ethanol + Water Binary Mixtures from (293.2 to 333.2) K
• Solubility of Genistein in Water, Methanol, Ethanol, Propan-2-ol, 1-Butanol, and Ethyl Acetate from (280 to 333) K
• Solubilities of Phosphorus-Containing Compounds in Selected Solvents
• 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
• Determination of Activity Coefficients at Infinite Dilution of 35 Solutes in the Ionic Liquid, 1-Butyl-3-methylimidazolium Tosylate, Using Gas-Liquid Chromatography
• Experimental Isobaric Vapor-Liquid Equilibrium for Binary Systems of Ethyl Methyl Carbonate + Methanol, + Ethanol, + Dimethyl Carbonate, or + Diethyl Carbonate at 101.3 kPa
• Activity Coefficients at Infinite Dilution for Hydrocarbons in Fatty Alcohols Determined by Gas-Liquid Chromatography
• Vapor-Liquid Equilibria for Ethyl Acetate + Methanol at (0.1, 0.5, and 0.7) MPa. Measurements with a New Ebulliometer
• Solubility and Crystal Size of Sirolimus in Different Organic Solvents
• Solubility of Butyl Paraben in Methanol, Ethanol, Propanol, Ethyl Acetate, Acetone, and Acetonitrile
• Excess Molar Enthalpies of Methyl Acetoacetate + (Methanol, + Ethanol, + 1-Propanol, and + 2-Propanol) at T = (288.2, 298.2, 313.2, and 328.2) K and p = 101.3 kPa
• Solubility of Forms I and II of Clopidogrel Hydrogen Sulfate in Methanol and 2-Propanol Mixture
• Solubility of Florfenicol in Different Solvents at Temperatures from (278 to 318) K
• Volumetric Properties for (Ionic Liquid + Methanol or Ethanol or 1-Propanol + Nitromethane) at 298.15 K and Atmospheric Pressure
• Densities and Viscosities of Binary Mixture of the Ionic Liquid Bis(2-hydroxyethyl)ammonium Propionate with Methanol, Ethanol, and 1-Propanol at T = (293.15, 303.15, 313.15, and 323.15) K and at P = 0.1 MPa
• Measurement and Correlation of Solubilities of Cefpirome Sulfate in Aqueous Alcohol Solution between (278.15 and 308.15) K
• Measurement and Modeling of Liquid-Liquid Equilibrium for Ternary and Quaternary Mixtures of Water, Methanol, 2-Propanol, and 2,2,4-Trimethylpentane at 293.2 K
• Vapor-Liquid Equilibrium and Liquid-Liquid Equilibrium of Methyl Acetate + Methanol + 1-Ethyl-3-methylimidazolium Acetate
• Effect of the Ionic Liquid Triethylmethylammonium Dimethylphosphate on the Vapor Pressure of Water, Methanol, Ethanol, and Their Binary Mixtures
• Solubility of Dimethyl Fumarate in Methanol, Ethanol, 1-Propanol, 2-Propanol, 1,2-Propanediol, and Water from (289.95 to 347.15) K
• 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
• Excess Molar Enthalpies of 2-Methyl-2-butanol (1) + 1-Alkanols (C1-C5) (2) at 298.15 K
• Solubility of 2-Chloro-4,6-dinitroresorcinol in Ethanol, Methanol, Acetic Acid, Ethyl Acetate, and Water
• Ternary Liquid-Liquid Equilibria for the (Methanol + Methylbenzene + Decane) System at Different Temperatures
• Solubilities of Phloretin in 12 Solvents at Different Temperatures
• Density, Viscosity, and Thermal Conductivity of Mixtures of 1-Ethoxy-1,1,2,2,3,3,4,4,4-nonafluorobutane (HFE 7200) with Methanol and 1-Ethoxybutane
• Solid-Liquid Equilibria in Three Binary Mixtures Containing Diphenyl Carbonate
• Measurement and Correlation of the Solubility of Prednisone Acetate in Different Solvents
• Measurement and Correlation of Solubilities of Asiaticoside in Water, Methanol, Ethanol, n-Propanol, n-Butanol, and a Methanol + Water Mixture from (278.15 to 343.15) K
• Solubilities of Pioglitazone Hydrochloride in Different Solvents
• Solubility of Minoxidil in Methanol, Ethanol, 1-Propanol, 2-Propanol, 1-Butanol, and Water from (278.15 to 333.15) K
• Solubility of Imperatorin in Ethyl Acetate, Ethanol, Methanol, n-Hexane, and Petroleum Ether from (278.2 to 318.2) K
• Isothermal Vapor-Liquid Equilibrium for Methanol and 2,3-Dimethyl-1-butene at 343.06 K, 353.27 K, 363.19 K, and 372.90 K
• Solubilities of Ursolic Acid and Oleanolic Acid in Four Solvents from (283.2 to 329.7) K
• Experimental and Predicted (Vapor + Liquid) Equilibrium Data of Ternary Mixtures of Methanol, Water, and Propan-1,2,3-triol at 96 kPa
• 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 of Solubilities of (Z)-2-(2-Aminothiazol-4-yl)-2-methoxyiminoacetic Acid in Different Pure Solvents and Binary Mixtures of Water + (Ethanol, Methanol, or Glycol)
• 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
• Article Isobaric Vapor Liquid Equilibrium for Methanol + Methyl Acetate + 1-Octyl-3-methylimidazolium Hexafluorophosphate at 101.3 kPa
• Densities, Viscosities, and Refractive Properties of the Binary Mixtures of the Amino Acid Ionic Liquid [bmim][Ala] with Methanol or Benzylalcohol at T = (298.15 to 313.15) K
• Solubility of 2-(2,4,6-Trichlorophenoxy)ethyl Bromide in Methanol, Ethanol, Propanol, Isopropanol, Acetonitrile, n-Heptane, and Acetone
• Determination of Infinite Dilution Partial Molar Excess Enthalpies and Volumes for Some Ionic Liquid Precursors in Water and Methanol Using Tandem Flow Mixing Calorimetry and Vibrating-Tube Densimetry
• Vapor-Liquid Equilibrium for Methoxymethane + Methyl Formate, Methoxymethane + Hexane, and Methyl Formate + Methanol
• Partial Molar Volumes and Viscosity B-Coefficients of N,N'-Ethylene-bis(salicylideneiminato)cobalt(II) in Binary Mixtures of 1,4-Dioxane + Methanol at T = (298.15, 303.15, 308.15, and 313.15) K
• Activity Coefficients at Infinite Dilution of Organic Compounds in Four New Imidazolium-Based Ionic Liquids
• Influence of Some Ionic Liquids Containing the Trifluoromethanesulfonate Anion on the Vapor Liquid Equilibria of the Acetone + Methanol System
• Organic Salt Effect of Tetramethylammonium Bicarbonate on the Vapor Liquid Equilibrium of the Methanol Water System
• Effects of Concentration, Temperature, and Solvent Composition on the Partial Molar Volumes of Sodium Lauryl Sulfate in Methanol (1) + Water (2) Mixed Solvent Media
• Solubilities of Betulinic Acid in Thirteen Organic Solvents at Different Temperatures
• Isobaric Vapor Liquid Equilibrium for Methanol + Dimethyl Carbonate + 1-Octyl-3-methylimidazolium Tetrafluoroborate
• Viscosity and density measurement for six binary mixtures of water (methanol or ethanol) with an ionic liquid [BMIM][DMP] or [EMIM][DMP] at atmospheric pressure in the temperature range of (293.15 to 333.15) K
• Electrical Conductivity of Solutions of Ionic Liquids with Methanol, Ethanol, Acetonitrile, and Propylene Carbonate
• Activity Coefficients at Infinite Dilution by GLC in Alkanediamines as Stationary Phases
• Partition Coefficients of Organic Compounds in Four New Tetraalkylammonium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Using Inverse Gas Chromatography
• Liquid Liquid Equilibria of Methanol, Ethanol, and Propan-2-ol with Water and Dodecane
• Organic Salt Effect of Tetramethylammonium Bicarbonate on Vapor-Liquid Equilibrium of the Dimehyl Carbonate + Methanol System
• Density, Viscosity, and Refractive Index Properties for the Binary Mixtures of n-Butylammonium Acetate Ionic Liquid + Alkanols at Several Temperatures
• Interactions of Volatile Organic Compounds with the Ionic Liquid 1-Butyl-1-methylpyrrolidinium Dicyanamide
• Antisolvent Precipitation of Vitamin B6: A Thermodynamic Study
• Liquid liquid equilibrium for the ternary systems of water + methanol + acrylonitrile
• Liquid-Liquid Phase Behaviors of Geraniol in Aqueous Alcohol Mixtures
• 1-Ethyl-3-methylimidazolium Dicyanamide as a Very Efficient Entrainer for the Extractive Distillation of the Acetone + Methanol System
• Liquid-Liquid Equilibria for the System Dimethyl Carbonate + Methanol + Glycerol in the Temperature Range of (303.15 to 333.15) K
• Experimental Measurement and Modeling of Aniline Hydrochloride Solubility in Water, Methanol, Ethanol, 1- Propanol and Their Mixed Systems
• Densities and Viscosities for Binary Mixtures of the Ionic Liquid N-Ethyl Piperazinium Propionate with n-Alcohols at Several Temperatures
• Evaluation of the Performance of Trigeminal Tricationic Ionic Liquids for Separation Problems
• Excess Volumes of Ternary Mixtures 2,2,4-Trimethylpentane + Diisopropyl Ether or Methyl tert-Butyl Ether + Methanol, Ethanol, or 1-Propanol at 298.15 K
• Solubility of Thiotriazinone in Binary Solvent Mixtures of Water + Methanol and Water + Ethanol from (283 to 330) K
• Solubility and Solution Thermodynamics of Betaine in Different Pure Solvents and Binary Mixtures
• Vapor Liquid Equilibrium Data for Methanol + tert-Butylamine + N,N-Dimethylformamide and Constituent Binary Systems at Atmospheric Pressure
• Determination of Gas Concentrations in Liquids by Nuclear Magnetic Resonance: Hydrogen in Organic Solvents
• Solubility of 6-Chloropyridazin-3-amine in Different Solvents
• Measurement and Correlation of the Solubility of 2,6-Diaminohexanoic Acid Hydrochloride in Aqueous Methanol and Aqueous Ethanol Mixtures
• Solubilities of 3-Methoxy-N-phenylaniline and 3-(Methylthio)-N-phenylaniline in Five Organic Solvents (285 K to 333.75 K)
• On the Solubility of Carbon Dioxide in Binary Water Methanol Mixtures
• Electrical Conductances of 1-Butyl-3-propylimidazolium Bromide and 1-Butyl-3-propylbenzimidazolium Bromide in Water, Methanol, and Acetonitrile at (308, 313, and 318) K at 0.1 MPa
• Solubilities of Bis(2,4,6-trimethylbenzoyl)phenylphosphine Oxide in Different Organic Solvents at Several Temperatures
• Solubility of Vitamin D3 in Six Organic Solvents at Temperatures from (248.2 to 273.2) K
• Solubility of Benzoic Acid in Mixtures of CO2 + Hexane
• Determination and Correlation of Pyridazin-3-amine Solubility in Eight Organic Solvents at Temperatures Ranging from (288.05 to 333.35) K
• Biomass-Derived Platform Chemicals: Thermodynamic Studies on the Extraction of 5-Hydroxymethylfurfural from Ionic Liquids
• Viscosimetric Study of Binary Mixtures Containing Pyridinium-Based Ionic Liquids and Alkanols
• Ternary and Quaternary Liquid Liquid Equilibria for Systems of Water + Methanol + Methylanthranilate + Toluene at Different Temperatures
• Organic Salt Effect on Vapor Liquid Equilibrium of the Methanol + Water System at Subatmospheric Pressure
• Measurement and Correlation of the Solubility of Febuxostat in Four Organic Solvents at Various Temperatures
• Activity Coefficients at Infinite Dilution for Organic Compounds Dissolved in 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Having Six-, Eight-, and Ten-Carbon Alkyl Chains
• Isobaric Vapor Liquid Equilibrium Data of 2-Methyl-propan-2-ol (1) + Heptan-1-ol (2), Methanol (1) + Heptan-1-ol (2), Ethanol (1) + Heptan-1-ol (2), and Propan-1-ol (1) + Heptan-1-ol (2) at 96.5 kPa
• Solubility, Density and Solution Thermodynamics of NaI in Different Pure Solvents and Binary Mixtures
• Vapor Liquid Equilibrium at p/kPa = 101.3 of the Binary Mixtures of Ethenyl Acetate with Methanol and Butan-1-ol
• Solubility and Induction Period Study of Asiaticoside and Madecassoside in a Methanol + Water Mixture
• Synthesis and Physicochemical Properties of Amino Acid Ionic Liquid 1-Butyl-3-methylimidazolium Aspartate and Binary Mixture with Methanol
• 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
• Effect of Ionic Liquids on the Isobaric Vapor-Liquid equilibrium behavior of methanol-methyl ethyl ketone (MEK)
• Isobaric Vapor Liquid Equilibrium for the Binary Systems of Methanol, Diethylamine, and N,N-Diethylethanolamine at p = (60.0 and 101.3) kPa
• Investigation of the Solubility of Octahydro-1,3,5,7-tetranitro-1,3,5,7-tetrazocine and 1,3,5-Triacetyl-hexahydro-s-triazine
• Solubilities of 4,4'-Dichlorodiphenyl Disulfide in Six Organic Solvents between (303.15 and 333.15) K
• Isobaric Vapor Liquid Equilibrium for Methanol + Dimethyl Carbonate + 1-Butyl-3-methylimidazolium Dibutylphosphate
• Densities and Excess Properties of Primary Amines in Alcoholic Solutions
• Ionic Conductivities of Binary Mixtures Containing Pyridinium-Based Ionic Liquids and Alkanols
• Surface Tension Measurements for Seven Imidazolium-Based Dialkylphosphate Ionic Liquids and Their Binary Mixtures with Water (Methanol or Ethanol) at 298.15 K and 1 atm
• Isothermal Vapor Liquid Equilibrium Data for the Butan-2-one + Methanol or Ethanol Systems Using a Static-Analytic Microcell
• Solubilities of Rutaecarpine in Twelve Organic Solvents from (283.2 to 323.2) K
• Measurement and Prediction of Excess Enthalpies for Ternary Solutions 1-Ethyl-3-methylimidazolium Dimethylphosphate + Methanol or Ethanol + Water at 298.15 K and at Normal Atmospheric Pressure
• Determination and Correlation of Solubilities of (S)-Indoline-2-carboxylic Acid in Six Different Solvents from (283.15 to 358.15) K
• Activity Coefficients at Infinite Dilution for Organic Solutes Dissolved in Three 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Bearing Short Linear Alkyl Side Chains of Three to Five Carbons
• Determination and Correlation of Solubility of Cefradine Form I in Five Pure Solvents from (283.15 to 308.15) K
• Experimental Measurements of Vapor Liquid Equilibrium Data for the Binary Systems of Methanol + 2-Butyl Acetate, 2-Butyl Alcohol + 2-Butyl Acetate, and Methyl Acetate + 2-Butyl Acetate at 101.33 kPa
• 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
• Isobaric Vapor Liquid Equilibrium for Chloroform + Methanol + 1,3-Dimethylimidazolium Dimethylphosphate at 101.3 kPa
• Solubilities of Phosphonic Acid, P,P'-(1,4-Piperazinediyl)bis-,P,P,P',P'-tetraphenyl Ester in Selected Solvents
• Solubility of 3,4-Dichloronitrobenzene in Methanol, Ethanol, and Liquid Mixtures (Methanol + Water, Ethanol + Water): Experimental Measurement and Thermodynamic Modeling
• Solubility of Hesperetin in Mixed Solvents
• Solubility of 3,4-Bis(3-nitrofurazan-4-yl)furoxan in Common Solvents at Temperatures between 293.15 K and 313.15 K
• Solubility of Sodium Acetate in Binary Mixtures of Methanol, 1-Propanol, Acetonitrile, and Water at 298.2 K
• Measurement and Correlation of Solubility of 2-Chloro-4-ethylamino-6-isopropylamino-1,3,5-triazine in Different Organic Solvents
• Vapor Liquid Equilibrium of Methane with Water and Methanol. Measurements and Modeling
• Liquid Liquid Equilibria for Ternary Mixtures of Methylphenyl Carbonate, Dimethyl Carbonate, Diphenyl Carbonate, Anisole, Methanol, Phenol, and Water at Several Temperatures
• Measurement and Correlation of Solubilities of Indole-2-carboxylic Acid in Ten Different Pure Solvents from (278.15 to 360.15) K
• Solubility of 2-Hydroxypropane-1,2,3-tricarboxylic Acid Monohydrate in Different Binary Solvents from (278.15 to 303.15) K
• Solid Liquid Equilibrium of Theophylline in Solvent Mixtures
• Solubilities of 4-(Hydroxymethyl)-1-oxido-2,6,7-trioxa-1-phosphabicyclo[2.2.2]octane in Organic Solvents
• Thermodynamics of Fluconazole Solubility in Various Solvents at Different Temperatures
• 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
• Thermophysical Properties of the Binary Mixture 1-Propylpyridinium Tetrafluoroborate with Methanol
• Densities and Viscosities of Binary Mixtures Containing 1,3-Dimethylimidazolium Dimethylphosphate and Alcohols
• Experimental Measurements and Modeling of the Solubility of Aceclofenac in Six Pure Solvents from (293.35 to 338.25) K
• Infinite Dilution Activity Coefficients of Solutes Dissolved in Two Trihexyl(tetradecyl)phosphonium Ionic Liquids
• 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
• Determination and Correlation of Solubilities of Lauric Acid in Eight Alcohols
• Solubility of Aspartame in Water, Methanol, Ethanol and Different Binary Mixtures in the Temperature Range of (278.15 to 333.15) K
• 4-Amino-3,6-dichloropyridazine Solubility Measurement and Correlation in Seven Pure Organic Solvents from (278.15 to 333.15) K
• Measurement, Correlation, and Thermodynamics Parameters of Biological Active Pyrimidine Derivatives in Organic Solvents at Different Temperatures
• Solubility Determination of Tris(hydroxymethyl)aminomethane in Water + Methanol Mixtures at Various Temperatures Using a Laser Monitoring Technique
• Density, Viscosity, and Conductivity of Binary Mixtures of the Ionic Liquid N-(2-Hydroxyethyl)piperazinium Propionate with Water, Methanol, or Ethanol
• Solubility of Tetranitrodimerglycoluril (TNDGU) in Different Solvents at Temperatures between 293.15 K and 313.15 K
• Phase equilibrium study of binary and ternary mixtures of ionic liquids + acetone + methanol
• Thermodynamic Models for Determination of the Solubility of Dibenzothiophene in Different Solvents at Temperatures from (278.15 to 328.15) K
• Isobaric Vapor Liquid Equilibrium for Methanol + Dimethyl Carbonate + Trifluoromethanesulfonate-based Ionic Liquids at 101.3 kPa
• 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 in Ternary Systems of Hexafluoroisopropanol + Perfluorocarbon + Water or Methanol at 298.15 K
• Experimental Measurement and Modeling of Solubility Data for 2,3-Dichloronitrobenzene in Methanol, Ethanol, and Liquid Mixtures (Methanol + Water, Ethanol + Water)
• Experimental Measurement and Correlation of Solubility Data and Thermodynamic Properties of Protocatechuic Acid in Four Organic Solvents
• Liquid Liquid Equilibrium in Mixtures Containing Propane-1,2,3-triol and Mixtures Containing Vegetable Oils at Atmospheric Pressure
• Isobaric Vapor Liquid Equilibria for the Binary and Ternary Systems of Methanol, Epichlorohydrin, and Glycerol Dimethyl Ether at 101.3 kPa
• Liquid Liquid Equilibrium for Ternary System Methanol + Methyl Acetate + 1,3-Dimethylimidazolium Dimethylphosphate at Several Temperatures and Atmospheric Pressure
• Isobaric Vapor Liquid Equilibrium for Acetone + Methanol + Phosphate Ionic Liquids
• Solubility Measurement and Correlation for 3,5-Dichloroaniline in (Methanol + Water) and (Ethanol + Water) Mixed Solvents
• Speed of sound, density and related thermodynamic excess properties of binary mixtures of butan-2-one with C1-C4 nalkanols and chloroform
• Experimental Measurement and Modeling of the Solubility of Biotin in Six Pure Solvents at Temperatures from 298.15 K to 333.85 K
• Solubility and Thermodynamic Properties of (2S)-Pyrrolidine-2-carboxylic Acid in Water, Alcohols, and Water Alcohol Mixtures
• 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
• Thermodynamic Properties of Polymorphs of 2,2'-Thiodiethylene Bis[3-(3,5-di-tert-butyl-4-hydroxyphenyl)propionate]
• Liquid Liquid Equilibria of Three Ternary Systems: {Glycerol + Benzene + Methanol}, {Glycerol + Benzene + Ethanol}, and {Glycerol + Benzene + 1-Propanol}
• Thermal Stability and Vapor Liquid Equilibrium for Imidazolium Ionic Liquids as Alternative Reaction Media
• Solubility of Tris(hydroxymethyl)aminomethane in Methanol + 1-Propanol Mixtures at Various Temperatures
• Thermodynamic Models for Determination of the Solubility of the (1:1) Complex of (Urea + l-Malic Acid) in (Methanol + Acetonitrile) Binary Solvent Mixtures
• Density of Methanolic Alkali Halide Salt Solutions by Experiment and Molecular Simulation
• Experimental and Modeling Studies on the Solubility of d-Pantolactone in Four Pure Solvents and Ethanol Water Mixtures
• Solubility and Solution Thermodynamics of Diphenoxylate in Different Pure Solvents
• Solubilities of Naringin and Naringenin in Different Solvents and Dissociation Constants of Naringenin
• 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
• Vapor Pressures and Activity Coefficients of Methanol in Binary Mixtures with 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl)imide
• 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
• Measurement and Correlation of the Solubility for 4,4'-Diaminodiphenylmethane in Different Solvents
• Isobaric Vapor-Liquid Equilibria for Methyl Acetate + Methanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
• Vapor-Liquid Equilibrium of Mixtures Containing Adipic Acid, Glutaric Acid, Dimethyl Adipate, Dimethyl Glutarate, Methanol, and Water
• Physical Properties of Binary Mixtures of the Ionic Liquid 1-Ethyl-3-methylimidazolium Ethyl Sulfate with Several Alcohols at T = (298.15, 313.15, and 328.15) K and Atmospheric Pressure
• Experimental Investigation of the Solubility of Ammonia in Methanol
• Measurement and Prediction of Vapor Pressure of Binary and Ternary Systems Containing 1-Ethyl-3-methylimidazolium Ethyl Sulfate
• 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
• Volumetric and Ultrasonic Studies of 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate Ionic Liquid with Methanol, Ethanol, 1-Propanol, and Water at Several Temperatures
• Isothermal Vapor-Liquid Equilibrium Data for the System Methanol + Toluene + Triphenylbenzylphosphonium Chloride
• Solubility of Triethylenediamine in Methanol, Ethanol, Isopropanol, I-Butanol, and Ethyl Acetate between 276.15 K and 363.15 K
• Densities and Excess Volumes of the 1,3-Dimethylimidazolium Methylsulfate + Methanol System at Temperatures from (313.15 to 333.15) K and Pressures from (0.1 to 25) MPa
• Solubility of 1-H-Tetrazole-1-acetic Acid in Different Solvents between 283 K and 323 K
• Solubility of Phenacetinum in Methanol, Ethanol, 1-Propanol, 1-Butanol, 1-Pentanol, Tetrahydrofuran, Ethyl Acetate, and Benzene between 282.65 K and 333.70 K
• Solubility of 2,6-Diaminopyridine in Toluene, o-Xylene, Ethylbenzene, Methanol, Ethanol, 2-Propanol, and Sodium Hydroxide Solutions
• Thermodynamic Properties of 1-Butyl-3-methylpyridinium Tetrafluoroborate and Its Mixtures with Water and Alkanols
• Solubilities of the Gaseous and Liquid Solutes and Their Thermodynamics of Solubilization in the Novel Room-Temperature Ionic Liquids at Infinite Dilution by Gas Chromatography
• Solubilities of 2-Methyl-1,4-naphthoquinone in Water + (Methanol, Ethanol, 1-Propanol, 2-Propanol, 1,2-Propanediol, and Glycerin, Respectively) from (293.15 to 337.92) K
• Temperature Dependence of the Volumetric Properties of Binary and Ternary Mixtures of Water (1) + Methanol (2) + Ethanol (3) at Ambient Pressure (81.5 kPa)
• Ionic Conductivity of Selected 2:1 Electrolytes in Dilute Solutions of Mixed Aqueous Organic Solvents at 298.15 K
• Viscosity, Density, Speed of Sound, and Refractive Index of Binary Mixtures of Organic Solvent + Ionic Liquid, 1-Butyl-3-methylimidazolium Hexafluorophosphate at 298.15 K
• Binary LLE for Propyl Vinyl Ether (PVE) + Water, Ternary LLE for PVE + Methanol or Ethanol + Water at 298.15 K, and VE and centsR at 293.15 K for the Mixture of PVE + Ethanol + 2,2,4-Trimethylpentane
• Vapor Liquid Equilibrium for Butane + Methanol, + Ethanol, + 2-Propanol, + 2-Butanol, and + 2-Methyl-2-Propanol (TBA) at 323 K
• Liquid Liquid Equilibria of Mixtures Containing Methyl Acetate + Methanol + Hexane or Heptane
• 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
• Solubility of 2-(4-Ethylbenzoyl)benzoic Acid in Eleven Organic Solvents between 279.55 K and 343.15 K
• Volumetric Properties and Viscosities of Binary Mixtures of N,N-Dimethylformamide with Methanol and Ethanol in the Temperature Range (293.15 to 333.15) K
• Solubility of Dioxopromethazine Hydrochloride in Different Solvents
• Excess Enthalpies of 2,4-Pentanedione + (Methanol, + Ethanol, + 1-Propanol, and + 2-Propanol) at T = (298.15, 313.15, and 328.15) K and p = (0.1 and 10.0) MPa
• Solubility of Trimethoprim (TMP) in Different Organic Solvents from (278 to 333) K
• Naphthalene Solubility in Binary Solvent Mixtures of 2,2,4-Trimethylpentane + Alcohols at 298.15 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
• Measuring Surface Tension of Liquids at High Temperature and Elevated Pressure
• Solubility of Gallic Acid in Methanol, Ethanol, Water, and Ethyl Acetate
• 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
• Excess Molar Enthalpies of Acetophenone + (Methanol, + Ethanol, + 1-Propanol, and + 2-Propanol) at Different Temperatures and Pressures
• Vapor Liquid Equilibrium for the Systems trans-2-Butene + Methanol, + 1-Propanol, + 2-Propanol, + 2-Butanol, and + 2-Methyl-2-propanol at 364.5 K
• Solubility of Form r and Form a of Glycine in Aqueous Solutions
• Phase Equilibrium of Biodiesel Compounds for the Triolein + Palmitic Acid + Methanol System with Dimethyl Ether as Cosolvent
• Solubility of Acesulfame Potassium in Ethanol + Water and Methanol + Water Systems from (275.84 to 322.90) K
• Solubility of Losartan Potassium in Different Pure Solvents from (293.15 to 343.15) K
• Solubility of Rifapentine in Different Organic Solvents
• Vapor Liquid Equilibrium Behaviors of 5-Methyl-2-(1-methylethyl)phenol in Alcohol
• Vapor Liquid Equilibrium for the Systems 2-Methylpropane + Methanol, + 2-Propanol, + 2-Butanol, and + 2-Methyl-2-propanol at 364.5 K
• Solubilities of Menadione Sodium Bisulfite in Water + (Methanol, Ethanol, 1-Propanol, 2-Propanol, 1,2-Propanediol, and Glycerin, Respectively) from (297.67 to 337.76) K
• Densities, Viscosities, and Liquid Diffusivities in Aqueous Piperazine and Aqueous (Piperazine + N-Methyldiethanolamine) Solutions
• 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 Hesperetin in Various Solvents from (288.2 to 323.2) K
• Vapor-Liquid Equilibrium for the cis-2-Butene + Methanol, + 2-Propanol, + 2-Butanol, + 2-Methyl-2-propanol Systems at 364.5 K
• Determination of Activity Coefficients at Infinite Dilution of Solutes in the Ionic Liquid, Trihexyltetradecylphosphonium Bis(trifluoromethylsulfonyl) Imide, Using Gas-Liquid Chromatography at T ) (303.15, 308.15, 313.15, and 318.15) K
• Vapor-Liquid Equilibrium Data for the System Methanol + Toluene + Tetrabutylammonium Tetraphenylborate
• Isobaric Vapor-Liquid Equilibria for Tetrahydropyran and Alcohol Systems
• Solubility of Isoniazid in Various Organic Solvents from (301 to 313) K
• Vapor-Liquid Equilibrium for 1-Butene + Methanol, + 1-Propanol, + 2-Propanol, + 2-Butanol, and 2-Methyl-2-propanol (TBA) at 364.5 K
• Excess Molar Volume and Viscosity Deviation for the Methanol + Methyl Methacrylate Binary System at T) (283.15 to 333.15) K
• Liquid-Liquid Equilibrium of (Cyclohexane + 2,2,2-Trifluoroethanol) and (Cyclohexane + Methanol) from (278.15 to 318.15) K
• Solubility of Pravastatin Sodium in Water, Methanol, Ethanol, 2-Propanol, 1-Propanol, and 1-Butanol from (278 to 333) K
• Solubility of Carbamazepine (Form III) in Different Solvents from (275 to 343) K
• 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 Clindamycin Phosphate in Methanol, Ethanol, and Dimethyl Sulfoxide
• Effect of Temperature on Phase Equilibrium of the Mixed-Solvent System of (2,2,2-Trifluoroethanol + Methanol + Cyclohexane)
• Solubility of 1-(2-Dimethylaminoethyl)-5-mercapto-1H-tetrazole in Water, DMF, Methanol, Ethanol, 1-Propanol, 2-Propanol, 1-Butanol, and 2-Butanol between (293 and 343) K
• Excess Molar Enthalpies of N,N-Dimethylethanolamine with (Methanol, Ethanol, 1-Propanol, and 2-Propanol) at T ) (298.2, 313.2, and 328.2) K and p ) (0.1 and 10.0) MPa
• Measurement and Correlation of the Surface Tension-Temperature Relation for Methanol
• Activity Coefficients at Infinite Dilution of Alkanols in the Ionic Liquids 1-Butyl-3-methylimidazolium Hexafluorophosphate, 1-Butyl-3-methylimidazolium Methyl Sulfate, and 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Amide Using the Dilutor Technique
• Temperature Dependence on Mutual Solubility Data of the Binary (Methanol + r-Pinene or -Pinene) Systems and Ternary Liquid-Liquid Equilibria for the (Methanol + Ethanol + r-Pinene or -Pinene) Systems
• Binary Liquid-Liquid Equilibrium (LLE) for Dibutyl Ether (DBE) + Water from (288.15 to 318.15) K and Ternary LLE for Systems of DBE + C1 !less thanless than C4 Alcohols + Water at 298.15 K
• Density, Ultrasonic Velocity, Electrical Conductivity, Viscosity, and Raman Spectra of Methanolic Mg(ClO4)2, Mg(NO3)2, and Mg(OAc)2 Solutions
• Conductivities of Binary Mixtures of Ionic Liquids with Polar Solvents
• Solubilities of Salicylic Acid in Pure Solvents and Binary Mixtures Containing Cosolvent
• Solubility of D(-)-p-Hydroxyphenylglycine Dane Salt in Eight Alcohols between (293 and 343) K
• Solubility of Artemisinin in Seven Different Pure Solvents from (283.15 to 323.15) K
• Measurement and Correlation of the Solubilities of m-Phthalic Acid in Monobasic Alcohols
• Effect of Dissolved Salts on the Enthalpy of Mixing of the Methanol + Formic Acid System at 303.15 K
• Solubility of Diphenyl Carbonate in Pure Alcohols from (283 to 333) K
• Cosolvent Effect of Methanol and Acetic Acid on Dibenzofuran Solubility in Supercritical Carbon Dioxide
• Solubility of Enrofloxacin Sodium in Various Solvents at Various Temperatures
• Solubility of Desmosterol in Five Organic Solvents
• Volumetric and Viscometric Studies of Salicyl Amide, Salicylic Acid, and Acetyl Salicylic Acid in Alcohols at Different Temperatures
• Solubility of Ammonium Thiocyanate in Different Solvents
• Densities, Excess Molar Volumes, Viscosity, and Refractive Indices of Binary and Ternary Liquid Mixtures of Methanol (1) + Ethanol (2) + 1,2-Propanediol (3) at P = 81.5 kPa
• Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Inverse Gas Chromatography
• Solubility of Hexamethylenetetramine in a Pure Water, Methanol, Acetic Acid, and Ethanol + Water Mixture from (299.38 to 340.35) K
• Solubility of Salol in Pure Alcohols from (283.15 to 308.15) K
• Binary Liquid-Liquid Equilibrium (LLE) for Methyl tert-Amyl Ether (TAME) + Water from (288.15 to 313.15) K and Ternary LLE for Systems of TAME + C1-C4 Alcohols + Water at 298.15 K
• Solubility of Podophyllotoxin in Six Organic Solvents from (283.2 to 323.2) K
• Solubility of Cloxacillin Sodium in Different Binary Solvents
• Solubility of Difloxacin in Acetone, Methanol, and Ethanol from (293.15 to 313.15) K
• Activity Coefficients at Infinite Dilution of Organic Compounds in Trihexyl(tetradecyl)phosphonium Bis(trifluoromethylsulfonyl)imide Using Inverse Gas Chromatography
• Solubility of Canthaxanthin in Pure Solvents from (293.15 to 343.15) K
• 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
• Diffusion Coefficients of 1-Alkyl-3-methylimidazolium Ionic Liquids in Water, Methanol, and Acetonitrile at Infinite Dilution
• Solubilities of Isonicotinic Acid in (Methanol, Ethanol, 1-Propanol, 2-Propanol, and 1,2-Propanediol, Respectively) from (289.65 to 358.75) K
• Temperature and Composition Dependence of the Density and Viscosity of Binary Mixtures of {1-Butyl-3-methylimidazolium Thiocyanate + 1-Alcohols}
• Paramagnetic Ionic Liquid 1-Butyl-3-methylimidazolium Tetrabromidocobaltate(II): Activity Coefficients at Infinite Dilution of Organic Solutes and Crystal Structure
• Densities and Viscosities of Binary Mixtures of Cyclopropanecarboxylic Acid with Methanol, Ethanol, Propan-1-ol, and Butan-1-ol at Different Temperatures
• Solubility of -Artemether in Methanol + Water and Ethanol + Water from (288.85 to 331.95) K
• Solubility of Tobramycin in Methanol, Ethanol, Dimethyl Sulfoxide, and N,N-Dimethylformamide
• Solubility of l-Lysine Hydrochloride in Dimethyl Sulfoxide, Methanol, Ethanol, Water, and Glycol between (283 and 323) K
• Solubility of Phenanthrene in Binary Mixtures of C1-C4 Alcohols + 2-Propanol and Ethanol + Methanol at 298.15 K
• Solubility and Liquid-Liquid Equilibrium of Aqueous Systems of Iodoethane with Methanol, Ethanol, or 1-Propanol at Temperature 298.15 K and Pressure 101.2 kPa
• Solubility of Baicalin in Methanol, Ethanol, and Ethyl Acetate from (298.2 to 328.2) K
• Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
• Solubilities of Some Chlorophenols in Supercritical CO2 in the Presence and Absence of Cosolvents
• Solubility of 2,6-Diamino-3,5-dinitropyridine and 2,5-Dihydroxyterephthalic Acid in N,N-Dimethylformamide, Dimethylsulfoxide, Ethanol, and Methanol, N,N-Dimethylacetamide, and Acetic Acid
• Excess Molar Enthalpies of Diethyl Malonate + (Methanol, + Ethanol, + 1-Propanol, and + 2-Propanol) at T = (288.2, 298.2, 313.2, and 328.2) K and p = 101.3 kPa
• Solubilities of 3,9-Dimethyl-3,9-dioxide-2,4,8,10-tetraoxa-3,9-diphosphaspiro[5.5]undecane in Selected Solvents
• Solubility of Irganox 1010 in (Alcohol + Water) Mixtures from (293.15 to 333.15) K
• Densities, Sound Speed, and IR Studies of (Methanol + 1-Acetoxybutane) and (Methanol + 1,1-Dimethylethyl Ester) at (298.15, 303.15, 308.15, and 313.15) K
• Solubility of Adenosine 5'-Monophosphate in Different Solvents from (288.15 to 330.15) K
• Solubility of Cytidine 5'-Diphosphocholine Sodium in Water and Different Binary Mixtures from (278.15 to 298.15) K
• Molar Conductivities and Association Constants of 1-Butyl-3-methylimidazolium Chloride and 1-Butyl-3-methylimidazolium Tetrafluoroborate in Methanol and DMSO
• Partial Molar Volumes of Butyltriethylammonium Iodide in Single Nonaqueous Solvents at 298.15 K
• Solubility of Camellianin A in Methanol, Acetonitrile, Acetone, and Water from (283.2 to 313.2) 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
• Excess Molar Enthalpies of Dibromomethane with Benzene, Methanol, Dimethylsulfoxide, and Pyrrolidin-2-one at 303.15 K
• Isobaric Vapor-Liquid and Liquid-Liquid Equilibria for Chloroform + Methanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
• Solubility of Phenanthrene in Binary Mixtures of C1-C4 Alcohols at 298.2 K
• Refractive Indices and Deviations in Refractive Indices for Binary Mixtures of 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate with Methanol, Ethanol, 1-Propanol, and 2-Propanol at Several Temperatures
• Solubilities of N-[(4-Bromo-3,5-difluorine)phenyl]acrylamide in Benzene, Methanol, Pyridine, Ethanol, Acetonitrile, and Toluene at Temperatures between (284.65 and 348.95) K
• Measurement and Correlation of Solubility of Pimelic Acid in Ether, Tetrahydrofuran, Ethanol, and Methanol
• Solubility of 5-Amino Salicylic Acid in Different Solvents at Various Temperatures
• Ion-Solvent Interactions of Some Halides of Common Cations with Organic Solvent Mixtures by Conductometric, Volumetric, Viscometric, and Refractometric Techniques
• Solubility of Flurbiprofen in CO2 and CO2 + Methanol
• 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
• Thermodynamic Properties of Inorganic Salts in Nonaqueous Solvents. VI. Apparent Molar Volumes, Expansibilities, and Compressibilities of Divalent Transition Metal Ions in Methanol and Dimethylsulfoxide
• Volumetric Properties of Binary Mixtures of 1-Butyl-3-methylimidazolium Chloride + Water or Hydrophilic Solvents at Different Temperatures
• Solubilities of Sulfadiazine in Methanol, Ethanol, 1-Propanol, 2-Propanol, Acetone, and Chloroform from (294.15 to 318.15) K
• Dissociation Constant of Quinic Acid and Association Constants of Some Quinates in Aqueous and in Alcoholic-Aqueous Mixed Solvents
• Solubility of Avermectin B1a in Some Pure and Mixed Solvents from (278.2 to 318.2) K
• Solid-Liquid Phase Diagram for the System MgCl2-NH3-CH3OH at 298 K
• Study of Ether-, Alcohol-, or Cyano-Functionalized Ionic Liquids Using Inverse Gas Chromatography
• Solubility of Sucralose in Different Solvents from (283.15 to 333.15) K
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Ethyl-3-methylimidazolium Tris(pentafluoroethyl)trifluorophosphate [EMIM][FAP] Using Gas-Liquid Chromatography
• Solubility of Delphinidin in Water and Various Organic Solvents between (298.15 and 343.15) K
• Solubility of Anthracene in Binary and Ternary Mixtures of Cyclohexanone, Ethyl Acetate, and Methanol at 298.2 K
• Isothermal Vapor-Liquid Equilibrium Data at T = 333.15 K and Excess Molar Volumes and Refractive Indices at T = 298.15 K for the Dimethyl Carbonate + Methanol and Isopropanol + Water with Ionic Liquids
• Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Hexyl-3-methylimidazolium Thiocyanate
• Ternary Excess Molar Volumes of {Methyltrioctylammonium Bis[(trifluoromethyl)sulfonyl]imide + Methanol + Methyl Acetate or Ethyl Acetate} Systems at (298.15, 303.15, and 313.15) K
• Determination and Correlation of the Solubility for Taurine in Water and Organic Solvent Systems
• ss-Sitosterol Solubility in Selected Organic Solvents
• Solubility of Quercetin in Water + Methanol and Water + Ethanol from (292.8 to 333.8) K
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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