Chemical Properties of Trichloromethane (CAS 67-66-3)

InChI

InChI=1S/CHCl3/c2-1(3)4/h1H

InChI Key

HEDRZPFGACZZDS-UHFFFAOYSA-N

Formula

CHCl3

SMILES

ClC(Cl)Cl

Molecular Weight¹

119.38

CAS

67-66-3

Other Names

• CHCl3
• Chloroforme
• Cloroformio
• F 20
• Formyl trichloride
• Methane trichloride
• Methane, trichloro-
• Methenyl trichloride
• Methyl trichloride
• NCI-C02686
• NSC 77361
• R 20
• R 20 (refrigerant)
• R-20
• Rcra waste number U044
• Trichloormethaan
• Trichlormethan
• Trichloroform
• Triclorometano
• UN 1888
• chloroform
• freon 20

• ω : Acentric Factor.
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• EA : Electron affinity (eV).
• ε_r : Dielectric Constant (Relative permittivity).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• R_g : Radius of Gyration.
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• ν : Kinematic viscosity (m²/s).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• NFPA Health : NFPA Health Rating.
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_c : Critical density (kg/m³).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I_p : Polar retention indices.
• c_sound,fluid : Speed of sound in fluid (m/s).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_boil(P) : Boiling point at given pressure (K).
• T_c : Critical Temperature (K).
• λ_gas : Gas thermal conductivity (W/m×K).
• λ_liquid : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• U_Qi : UNIQUAC Qi Parameter.
• U_Ri : UNIQUAC Ri Parameter.
• 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	[0.2160; 0.2260]
ω	0.2160		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.2260		ChemSep v8.3 pure component data Compiled value
ω	0.2180		KDB
ΔcH°liquid	[-474.00; -473.21]	kJ/mol
ΔcH°liquid	-473.21	kJ/mol	NIST
ΔcH°liquid	-474.00 ± 8.40	kJ/mol	NIST
μ	[1.01; 1.10]	debye
μ	1.01	debye	ChemSep v8.3 pure component data Compiled value
μ	1.10	debye	KDB
EA	[0.62; 1.76]	eV
EA	0.62 ± 0.16	eV	NIST
EA	1.76 ± 0.05	eV	NIST
εr	4.81		NCMS SOLV-DB
ΔfG°	[-70.10; -68.58]	kJ/mol
ΔfG°	-70.10	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	-68.58	kJ/mol	KDB
Rg	3.1780		KDB
ΔfH°gas	[-103.51; -101.30]	kJ/mol
ΔfH°gas	-103.51 ± 0.66	kJ/mol	Active Thermochemical Tables 1.112, gas-phase enthalpies of formation Compiled value
ΔfH°gas	-102.90	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-101.30	kJ/mol	KDB
ΔfH°gas	-102.90 ± 2.50	kJ/mol	NIST
ΔfH°liquid	[-134.30; -134.10]	kJ/mol
ΔfH°liquid	-134.10 ± 2.50	kJ/mol	NIST
ΔfH°liquid	-134.30	kJ/mol	NIST
ΔfusH°	7.41	kJ/mol	Joback Calculated Property
ΔvapH°	[30.50; 33.35]	kJ/mol
ΔvapH°	33.35	kJ/mol	NCMS SOLV-DB
ΔvapH°	31.40	kJ/mol	NIST
ΔvapH°	31.32 ± 0.08	kJ/mol	NIST
ΔvapH°	31.10	kJ/mol	NIST
ΔvapH°	30.50 ± 0.42	kJ/mol	NIST
IE	[11.30; 11.50]	eV
IE	11.37 ± 0.02	eV	NIST
IE	11.41 ± 0.02	eV	NIST
IE	11.30	eV	NIST
IE	11.48	eV	NIST
IE	11.37 ± 0.02	eV	NIST
IE	11.40	eV	NIST
IE	11.50	eV	NIST
IE	11.42 ± 0.03	eV	NIST
IE	11.50	eV	NIST
IE	11.48	eV	NIST
log10WS	[-1.17; -1.17]
log10WS	-1.17		Aq. Solubility Prediction
log10WS	-1.17		Estimated Solubility
logPoct/wat	1.970		NCMS SOLV-DB
McVol	61.670	ml/mol	McGowan Calculated Property
NFPA Health	2		KDB
Pc	[5328.68; 5500.00]	kPa
Pc	5330.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 10 Compiled value
Pc	5471.55	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	5500.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	5470.00	kPa	KDB
Pc	5328.68 ± 10.13	kPa	NIST
Pc	5328.68 ± 6.07	kPa	NIST
Ptriple	0.07	kPa	ChemSep v8.3 pure component data Compiled value
ρc	[458.41; 495.42]	kg/m3
ρc	490.64 ± 3.58	kg/m3	NIST
ρc	458.41 ± 2.39	kg/m3	NIST
ρc	495.42 ± 2.39	kg/m3	NIST
Inp	[561.00; 630.00]
Inp	617.20		NIST
Inp	619.00		NIST
Inp	628.40		NIST
Inp	625.80		NIST
Inp	621.10		NIST
Inp	618.20		NIST
Inp	614.80		NIST
Inp	607.90		NIST
Inp	604.00		NIST
Inp	606.00		NIST
Inp	604.00		NIST
Inp	606.80		NIST
Inp	610.00		NIST
Inp	604.00		NIST
Inp	608.00		NIST
Inp	602.00		NIST
Inp	Outlier 582.00		NIST
Inp	609.00		NIST
Inp	Outlier 568.00		NIST
Inp	595.20		NIST
Inp	616.00		NIST
Inp	610.00		NIST
Inp	587.00		NIST
Inp	622.00		NIST
Inp	622.00		NIST
Inp	613.00		NIST
Inp	598.00		NIST
Inp	601.00		NIST
Inp	616.00		NIST
Inp	615.00		NIST
Inp	601.00		NIST
Inp	621.70		NIST
Inp	601.00		NIST
Inp	590.00		NIST
Inp	618.00		NIST
Inp	600.00		NIST
Inp	Outlier 561.00		NIST
Inp	Outlier 569.00		NIST
Inp	630.00		NIST
Inp	605.00		NIST
Inp	615.00		NIST
Inp	601.00		NIST
Inp	615.00		NIST
Inp	618.00		NIST
Inp	618.00		NIST
Inp	600.00		NIST
Inp	588.00		NIST
Inp	601.00		NIST
Inp	616.00		NIST
Inp	609.00		NIST
Inp	617.00		NIST
Inp	609.00		NIST
Inp	609.00		NIST
Inp	611.00		NIST
Inp	629.00		NIST
Inp	609.00		NIST
Inp	603.00		NIST
Inp	620.00		NIST
Inp	618.00		NIST
Inp	609.00		NIST
Inp	601.00		NIST
Inp	601.00		NIST
Inp	603.00		NIST
Inp	605.00		NIST
Inp	620.00		NIST
Inp	609.00		NIST
Inp	611.00		NIST
Inp	601.00		NIST
Inp	606.00		NIST
Inp	603.00		NIST
Inp	609.00		NIST
Inp	616.00		NIST
Inp	595.00		NIST
Inp	605.00		NIST
Inp	605.00		NIST
Inp	615.00		NIST
Inp	618.00		NIST
Inp	598.00		NIST
Ip	[992.00; 1045.00]
Ip	1037.00		NIST
Ip	1037.00		NIST
Ip	1034.00		NIST
Ip	1030.11		NIST
Ip	1028.95		NIST
Ip	1027.69		NIST
Ip	1026.00		NIST
Ip	1026.00		NIST
Ip	1024.00		NIST
Ip	1021.00		NIST
Ip	1020.00		NIST
Ip	1022.00		NIST
Ip	1026.00		NIST
Ip	1026.00		NIST
Ip	1013.00		NIST
Ip	1028.00		NIST
Ip	1010.00		NIST
Ip	1020.00		NIST
Ip	1021.00		NIST
Ip	1022.00		NIST
Ip	1022.00		NIST
Ip	1018.00		NIST
Ip	1020.00		NIST
Ip	1023.00		NIST
Ip	1022.00		NIST
Ip	Outlier 999.00		NIST
Ip	1038.00		NIST
Ip	1010.00		NIST
Ip	Outlier 1045.00		NIST
Ip	1007.00		NIST
Ip	1037.00		NIST
Ip	1037.00		NIST
Ip	1017.00		NIST
Ip	1025.00		NIST
Ip	1015.00		NIST
Ip	1016.00		NIST
Ip	1037.00		NIST
Ip	1037.00		NIST
Ip	1018.00		NIST
Ip	1020.00		NIST
Ip	Outlier 992.00		NIST
Ip	1014.00		NIST
Ip	1014.00		NIST
Ip	Outlier 1000.00		NIST
Ip	Outlier 1000.00		NIST
Ip	1024.00		NIST
Ip	1037.00		NIST
Ip	1027.69		NIST
Ip	1010.00		NIST
Ip	1021.00		NIST
Ip	1013.00		NIST
Ip	1022.00		NIST
Ip	1014.00		NIST
Ip	1024.00		NIST
Tboil	[333.95; 335.00]	K
Tboil	Outlier 335.00	K	The role of organic diluents in the aspects of equilibrium, kinetics and thermodynamic model for silver ion extraction using an extractant D2EHPA
Tboil	334.10	K	Phase diagrams of (vapour + liquid) equilibrium for binary mixtures of a,a,a-trifluorotoluene with ethanol, or benzene, or chloroform at pressure 101.4 kPa
Tboil	334.35	K	Separation of azeotrope (2,2,3,3-tetrafluoro-1-propanol + water): Isobaric vapour-liquid phase equilibrium measurements and azeotropic distillation
Tboil	334.12	K	Isobaric Vapor-Liquid Phase Equilibrium Measurements for Allyl Alcohol with Chloroform, Ethyl Acetate, and Methyl Propionate at 101.3 kPa
Tboil	334.33	K	ChemSep v8.3 pure component data Compiled value
Tboil	334.32	K	KDB
Tboil	334.33	K	NCMS SOLV-DB
Tboil	334.30	K	NIST
Tboil	334.37 ± 0.15	K	NIST
Tboil	334.45 ± 0.50	K	NIST
Tboil	334.10 ± 0.30	K	NIST
Tboil	334.35 ± 0.06	K	NIST
Tboil	334.34 ± 0.25	K	NIST
Tboil	334.39 ± 0.30	K	NIST
Tboil	334.30 ± 0.20	K	NIST
Tboil	334.35 ± 0.10	K	NIST
Tboil	334.24 ± 0.15	K	NIST
Tboil	Outlier 333.95 ± 0.40	K	NIST
Tboil	334.42 ± 0.35	K	NIST
Tboil	334.42 ± 0.30	K	NIST
Tboil	334.35 ± 0.30	K	NIST
Tboil	334.35 ± 0.30	K	NIST
Tboil	334.35 ± 0.30	K	NIST
Tboil	334.30 ± 0.20	K	NIST
Tboil	334.30 ± 0.50	K	NIST
Tboil	334.45 ± 0.50	K	NIST
Tboil	334.20 ± 1.00	K	NIST
Tboil	334.50 ± 0.20	K	NIST
Tboil	334.22 ± 0.50	K	NIST
Tboil	334.27 ± 0.30	K	NIST
Tboil	334.30 ± 0.25	K	NIST
Tboil	334.30 ± 0.50	K	NIST
Tboil	334.23 ± 0.06	K	NIST
Tboil	334.30 ± 0.30	K	NIST
Tboil	334.40 ± 0.50	K	NIST
Tboil	334.37 ± 0.20	K	NIST
Tboil	334.20 ± 0.30	K	NIST
Tboil	334.22 ± 0.20	K	NIST
Tboil	334.35 ± 0.30	K	NIST
Tboil	334.30 ± 0.50	K	NIST
Tboil	334.15 ± 0.50	K	NIST
Tboil	334.40 ± 0.30	K	NIST
Tboil	334.35 ± 0.20	K	NIST
Tboil	334.45 ± 0.60	K	NIST
Tc	[535.65; 538.90]	K
Tc	536.20	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 10 Compiled value
Tc	536.40	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	536.50	K	ChemSep v8.3 pure component data Compiled value
Tc	536.40	K	KDB
Tc	536.40	K	NIST
Tc	Outlier 538.90 ± 0.80	K	NIST
Tc	536.10 ± 0.20	K	NIST
Tc	536.05 ± 0.50	K	NIST
Tc	536.30 ± 0.25	K	NIST
Tc	535.65 ± 0.30	K	NIST
Tfus	[209.50; 212.15]	K
Tfus	210.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	209.63	K	ChemSep v8.3 pure component data Compiled value
Tfus	209.50	K	KDB
Tfus	209.95	K	Aq. Solubility Prediction
Tfus	209.63	K	NCMS SOLV-DB
Tfus	209.73 ± 0.01	K	NIST
Tfus	209.64 ± 0.10	K	NIST
Tfus	210.15 ± 1.00	K	NIST
Tfus	209.61 ± 0.08	K	NIST
Tfus	209.65 ± 0.20	K	NIST
Tfus	211.05 ± 0.30	K	NIST
Tfus	209.50 ± 0.70	K	NIST
Tfus	210.00 ± 2.00	K	NIST
Tfus	209.65 ± 0.20	K	NIST
Tfus	Outlier 211.59 ± 0.50	K	NIST
Tfus	209.90 ± 0.30	K	NIST
Tfus	Outlier 212.15 ± 1.00	K	NIST
Tfus	210.46 ± 0.20	K	NIST
Tfus	210.00 ± 2.00	K	NIST
Ttriple	[209.61; 209.71]	K
Ttriple	209.71	K	Staveley, Lobo and Calado (1981), triple points Compiled value
Ttriple	209.63	K	ChemSep v8.3 pure component data Compiled value
Ttriple	209.61 ± 0.20	K	NIST
UQi	2.34		ChemSep v8.3 pure component data Compiled value
URi	2.70		ChemSep v8.3 pure component data Compiled value
Vc	[0.239; 0.244]	m3/kmol
Vc	0.244	m3/kmol	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 10 Compiled value
Vc	0.239	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.240	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.239	m3/kmol	KDB
Vm	8.07e-05	m3/mol	Excess Gibbs energies and volumes of the ternary system chloroform + tetrahydrofuran + cyclohexane at 298.15 K
Zc	[0.2910000; 0.2960000]
Zc	0.2910000		IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 10 Compiled value
Zc	0.2960000		ChemSep v8.3 pure component data Compiled value
Zc	0.2931300		KDB
Zra	0.28		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[110.00; 139.70]	J/mol×K	[240.00; 330.00]
Cp,liquid	110.00	J/mol×K	240.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	110.00	J/mol×K	250.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	111.00	J/mol×K	260.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	112.00	J/mol×K	270.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	112.00	J/mol×K	273.15	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	112.00	J/mol×K	280.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	113.00	J/mol×K	290.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	116.20	J/mol×K	293.00	NIST
Cp,liquid	115.50	J/mol×K	293.20	NIST
Cp,liquid	117.10	J/mol×K	298.00	NIST
Cp,liquid	114.18	J/mol×K	298.00	NIST
Cp,liquid	113.00	J/mol×K	298.10	NIST
Cp,liquid	114.00	J/mol×K	298.15	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	114.25	J/mol×K	298.15	NIST
Cp,liquid	114.32	J/mol×K	298.15	NIST
Cp,liquid	114.35	J/mol×K	298.15	NIST
Cp,liquid	115.50	J/mol×K	298.15	NIST
Cp,liquid	113.85	J/mol×K	298.15	NIST
Cp,liquid	115.50	J/mol×K	298.15	NIST
Cp,liquid	113.73	J/mol×K	298.15	NIST
Cp,liquid	114.26	J/mol×K	298.15	NIST
Cp,liquid	113.20	J/mol×K	298.15	NIST
Cp,liquid	113.40	J/mol×K	300.00	NIST
Cp,liquid	114.00	J/mol×K	300.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	116.70	J/mol×K	303.00	NIST
Cp,liquid	114.00	J/mol×K	303.20	NIST
Cp,liquid	139.70	J/mol×K	303.60	NIST
Cp,liquid	116.00	J/mol×K	310.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	117.00	J/mol×K	320.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	119.00	J/mol×K	330.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
η	[0.0004710; 0.0007130]	Pa×s	[273.15; 318.15]
η	0.0007130	Pa×s	273.15	Density, Viscosity, Vapor-Liquid Equilibrium, and Excess Molar Enthalpy of [Chloroform + Methyl tert-Butyl Ether]
η	0.0006510	Pa×s	283.15	Density, Viscosity, Vapor-Liquid Equilibrium, and Excess Molar Enthalpy of [Chloroform + Methyl tert-Butyl Ether]
η	0.0006000	Pa×s	293.15	Density, Viscosity, Vapor-Liquid Equilibrium, and Excess Molar Enthalpy of [Chloroform + Methyl tert-Butyl Ether]
η	0.0005357	Pa×s	298.15	NCMS SOLV-DB
η	0.0005760	Pa×s	298.15	Density, Viscosity, Vapor-Liquid Equilibrium, and Excess Molar Enthalpy of [Chloroform + Methyl tert-Butyl Ether]
η	0.0005560	Pa×s	298.15	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
η	0.0005340	Pa×s	303.15	Densities, Viscosities, and Ultrasonic Velocity Studies of Binary Mixtures of Chloroform with Propan-1-ol and Butan-1-ol at (303.15 and 313.15) K
η	0.0005340	Pa×s	303.15	Densities, Viscosities, and Ultrasonic Velocity Studies of Binary Mixtures of Chloroform with Octan-1-ol and Decan-1-ol at (303.15 and 313.15) K
η	0.0005200	Pa×s	303.15	Studies of viscosities of dilute solutions of alkylamine in non-electrolyte solvents. II. Haloalkanes and other polar solvents
η	0.0005520	Pa×s	303.15	Density, Viscosity, Vapor-Liquid Equilibrium, and Excess Molar Enthalpy of [Chloroform + Methyl tert-Butyl Ether]
η	0.0005130	Pa×s	308.15	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
η	0.0004910	Pa×s	313.15	Densities, Viscosities, and Ultrasonic Velocity Studies of Binary Mixtures of Chloroform with Octan-1-ol and Decan-1-ol at (303.15 and 313.15) K
η	0.0004910	Pa×s	313.15	Densities, Viscosities, and Ultrasonic Velocity Studies of Binary Mixtures of Chloroform with Propan-1-ol and Butan-1-ol at (303.15 and 313.15) K
η	0.0004710	Pa×s	313.15	Studies of viscosities of dilute solutions of alkylamine in non-electrolyte solvents. II. Haloalkanes and other polar solvents
η	0.0005090	Pa×s	313.15	Density, Viscosity, Vapor-Liquid Equilibrium, and Excess Molar Enthalpy of [Chloroform + Methyl tert-Butyl Ether]
η	0.0004910	Pa×s	318.15	Density, Viscosity, Vapor-Liquid Equilibrium, and Excess Molar Enthalpy of [Chloroform + Methyl tert-Butyl Ether]
ΔfusH	[8.80; 8.80]	kJ/mol	[209.60; 209.60]
ΔfusH	8.80	kJ/mol	209.60	NIST
ΔfusH	8.80	kJ/mol	209.60	NIST
ΔvapH	[28.90; 35.00]	kJ/mol	[248.00; 501.00]
ΔvapH	31.80	kJ/mol	248.00	NIST
ΔvapH	35.00	kJ/mol	274.50	NIST
ΔvapH	32.50	kJ/mol	296.50	NIST
ΔvapH	30.90	kJ/mol	320.50	NIST
ΔvapH	29.71	kJ/mol	334.30	KDB
ΔvapH	29.24	kJ/mol	334.30	NIST
ΔvapH	30.80	kJ/mol	366.50	NIST
ΔvapH	30.40	kJ/mol	374.50	NIST
ΔvapH	28.90	kJ/mol	445.50	NIST
ΔvapH	30.10	kJ/mol	501.00	NIST
ν	[0.0000003; 0.0000004]	m2/s	[303.15; 313.15]
ν	0.0000004	m2/s	303.15	Densities, Viscosities, and Ultrasonic Velocity Studies of Binary Mixtures of Chloroform with Pentan-1-ol, Hexan-1-ol, and Heptan-1-ol at (303.15 and 313.15) K
ν	0.0000003	m2/s	313.15	Densities, Viscosities, and Ultrasonic Velocity Studies of Binary Mixtures of Chloroform with Pentan-1-ol, Hexan-1-ol, and Heptan-1-ol at (303.15 and 313.15) K
Pvap	[26.26; 129.28]	kPa	[298.15; 342.00]
Pvap	26.26	kPa	298.15	NCMS SOLV-DB
Pvap	32.19	kPa	303.15	Density, viscosity, isothermal (vapour + liquid) equilibrium, excess molar volume, viscosity deviation, and their correlations for chloroform + methyl isobutyl ketone binary system
Pvap	32.41	kPa	303.15	Total Vapor Pressure Measurements for 2-Ethoxyethanol with Carbon Tetrachloride, Chloroform, and Dichloromethane at 303.15 K
Pvap	32.19	kPa	303.15	Density, Viscosity, Vapor-Liquid Equilibrium, Excess Molar Volume, Viscosity Deviation, and Their Correlations for the Chloroform + 2-Butanone Binary System
Pvap	34.81	kPa	305.00	Isobaric Vapor-Liquid and Liquid-Liquid Equilibria for Chloroform + Ethanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
Pvap	42.47	kPa	310.00	Isobaric Vapor-Liquid and Liquid-Liquid Equilibria for Chloroform + Ethanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
Pvap	51.43	kPa	315.00	Isobaric Vapor-Liquid and Liquid-Liquid Equilibria for Chloroform + Ethanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
Pvap	61.85	kPa	320.00	Isobaric Vapor-Liquid and Liquid-Liquid Equilibria for Chloroform + Ethanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
Pvap	73.88	kPa	325.00	Isobaric Vapor-Liquid and Liquid-Liquid Equilibria for Chloroform + Ethanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
Pvap	87.71	kPa	330.00	Isobaric Vapor-Liquid and Liquid-Liquid Equilibria for Chloroform + Ethanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
Pvap	101.30	kPa	334.12	Isobaric Vapor-Liquid Phase Equilibrium Measurements for Allyl Alcohol with Chloroform, Ethyl Acetate, and Methyl Propionate at 101.3 kPa
Pvap	101.30	kPa	334.35	Separation of azeotrope (2,2,3,3-tetrafluoro-1-propanol + water): Isobaric vapour-liquid phase equilibrium measurements and azeotropic distillation
Pvap	103.50	kPa	335.00	Isobaric Vapor-Liquid and Liquid-Liquid Equilibria for Chloroform + Ethanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
Pvap	121.45	kPa	340.00	Isobaric Vapor-Liquid and Liquid-Liquid Equilibria for Chloroform + Ethanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
Pvap	129.28	kPa	342.00	Isobaric Vapor-Liquid and Liquid-Liquid Equilibria for Chloroform + Ethanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
n0	[1.44100; 1.45000]		[283.15; 303.15]
n0	1.45000		283.15	Partial Molar Volumes of N,N'-1,2-Ethyl-bis(salicyladimine) Schiff Base (Salen) in Organic Solvents at T = (283.15 to 318.15) K
n0	1.44710		288.15	Partial Molar Volumes of N,N'-1,2-Ethyl-bis(salicyladimine) Schiff Base (Salen) in Organic Solvents at T = (283.15 to 318.15) K
n0	1.44760		293.15	Solubilities of Phosphorus-Containing Compounds in Selected Solvents
n0	1.44390		293.15	Partial Molar Volumes of N,N'-1,2-Ethyl-bis(salicyladimine) Schiff Base (Salen) in Organic Solvents at T = (283.15 to 318.15) K
n0	1.44280		298.15	Vapour pressure and excess Gibbs energy of binary 1,2-dichloroethane + cyclohexanone, chloroform + cyclopentanone and chloroform + cyclohexanone mixtures at temperatures from 298.15 to 318.15 K
n0	1.44200		298.15	Partial Molar Volumes of N,N'-1,2-Ethyl-bis(salicyladimine) Schiff Base (Salen) in Organic Solvents at T = (283.15 to 318.15) K
n0	1.44300		298.15	Liquid-Liquid Equilibrium, Solid-Liquid Equilibrium, Densities, and Refractivity of a Water, Chloroform, and Acetylacetone Mixture
n0	1.44290		298.15	Study of Vapor-Liquid Equilibrium for Binary Mixtures (Chloroform + 2,2,2-Trifluoroethanol) and (r,r,r-Trifluorotoluene + 2,2,2-Trifluoroethanol) at Pressure 102 kPa
n0	1.44200		298.15	NCMS SOLV-DB
n0	1.44100		303.15	Densities, speeds of sound, isentropic compressibilities, refractive indexes, and viscosities of tetrahydrofuran with haloalkane or alkyl ethanoate at T = 303.15 K
ρl	[1429.89; 1498.14]	kg/m3	[288.15; 323.15]
ρl	1498.08	kg/m3	288.15	Densities and Excess Molar Volumes of the Ternary Mixture 2-Butanol + Chloroform + Benzene and Binary Mixtures 2-Butanol + Chloroform, or + Benzene over the Temperature Range (288.15 to 313.15) K
ρl	1498.08	kg/m3	288.15	Temperature Dependence of Densities and Excess Molar Volumes of the Ternary Mixture (1-Butanol + Chloroform + Benzene) and its Binary Constituents (1-Butanol + Chloroform and 1-Butanol + Benzene)
ρl	1498.08	kg/m3	288.15	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
ρl	1498.14	kg/m3	288.15	Volumetric behaviour of binary mixtures of (trichloromethane + amines) at temperatures between T = (288.15 and 303.15) K at p = 0.1 MPa
ρl	1492.31	kg/m3	288.15	Densities and Excess Molar Volumes of the Binary Mixtures of Cyclopentanone with Chloroalkanes at T = (288.15, 298.15, 308.15, and 318.15) K
ρl	1491.86	kg/m3	288.15	Densities and Excess Molar Volumes of the Binary Mixtures of Cyclohexanone with Chloroalkanes at Temperatures between (288.15 and 318.15) K
ρl	1498.08	kg/m3	288.15	Volumetric properties of the ternary system ethanol + chloroform + benzene at temperature range (288.15 313.15) K: Experimental data, correlation and prediction by cubic EOS
ρl	1489.00	kg/m3	293.00	KDB
ρl	1488.64	kg/m3	293.15	Volumetric properties of the ternary system ethanol + chloroform + benzene at temperature range (288.15 313.15) K: Experimental data, correlation and prediction by cubic EOS
ρl	1488.70	kg/m3	293.15	Volumetric behaviour of binary mixtures of (trichloromethane + amines) at temperatures between T = (288.15 and 303.15) K at p = 0.1 MPa
ρl	1488.64	kg/m3	293.15	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
ρl	1488.70	kg/m3	293.15	Excess volumes, Viscosities, and Excess Gibbs Energy of Activation for Viscous Flow, for binary and ternary mixtures 1- propanol + N-N dimethylformamid + chloroform at different temperatures
ρl	1488.64	kg/m3	293.15	Temperature Dependence of Densities and Excess Molar Volumes of the Ternary Mixture (1-Butanol + Chloroform + Benzene) and its Binary Constituents (1-Butanol + Chloroform and 1-Butanol + Benzene)
ρl	1488.64	kg/m3	293.15	Densities and Excess Molar Volumes of the Ternary Mixture 2-Butanol + Chloroform + Benzene and Binary Mixtures 2-Butanol + Chloroform, or + Benzene over the Temperature Range (288.15 to 313.15) K
ρl	1487.63	kg/m3	293.15	Speed of sound, density and related thermodynamic excess properties of binary mixtures of butan-2-one with C1-C4 nalkanols and chloroform
ρl	1483.02	kg/m3	293.20	Isobaric vapour liquid equilibria for binary mixtures of 1,2-dibromoethane with 1,2-dichloroethane, trichloromethane, and 1,1,2,2-tetrachloroethane at atmospheric pressure
ρl	1478.16	kg/m3	298.15	Speed of sound, density and related thermodynamic excess properties of binary mixtures of butan-2-one with C1-C4 nalkanols and chloroform
ρl	1478.75	kg/m3	298.15	Densities, viscosities, and refractive indices of binary and ternary mixtures of methanol, acetone, and chloroform at temperatures from (298.15-318.15) K and ambient pressure
ρl	1479.15	kg/m3	298.15	Densities and Excess Molar Volumes of the Ternary Mixture 2-Butanol + Chloroform + Benzene and Binary Mixtures 2-Butanol + Chloroform, or + Benzene over the Temperature Range (288.15 to 313.15) K
ρl	1479.21	kg/m3	298.15	Volumetric behaviour of binary mixtures of (trichloromethane + amines) at temperatures between T = (288.15 and 303.15) K at p = 0.1 MPa
ρl	1473.16	kg/m3	298.15	Densities and Excess Molar Volumes of the Binary Mixtures of Cyclohexanone with Chloroalkanes at Temperatures between (288.15 and 318.15) K
ρl	1479.15	kg/m3	298.15	Volumetric properties of the ternary system ethanol + chloroform + benzene at temperature range (288.15 313.15) K: Experimental data, correlation and prediction by cubic EOS
ρl	1473.42	kg/m3	298.15	Volumetric Study for the Binary Nitromethane with Chloroalkane Mixtures at Temperatures in the Range (298.15 to 318.15) K
ρl	1479.15	kg/m3	298.15	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
ρl	1473.43	kg/m3	298.15	Densities and Excess Molar Volumes of the Binary Mixtures of Cyclopentanone with Chloroalkanes at T = (288.15, 298.15, 308.15, and 318.15) K
ρl	1479.15	kg/m3	298.15	Temperature Dependence of Densities and Excess Molar Volumes of the Ternary Mixture (1-Butanol + Chloroform + Benzene) and its Binary Constituents (1-Butanol + Chloroform and 1-Butanol + Benzene)
ρl	1480.34	kg/m3	298.20	The choice of solvent and liquid liquid equilibrium for ternary water + 2-methylaziridine + chloroform system: Experimental data and modeling
ρl	1475.30	kg/m3	303.00	Thermo-physical properties of 1,3,4-oxadiazole derivatives in pure solvents
ρl	1475.30	kg/m3	303.00	Thermo-acoustical studies of 1,3,4-oxadiazole as binary mixture at three different temperatures
ρl	1468.61	kg/m3	303.15	Speed of sound, density and related thermodynamic excess properties of binary mixtures of butan-2-one with C1-C4 nalkanols and chloroform
ρl	1469.16	kg/m3	303.15	Densities, viscosities, and refractive indices of binary and ternary mixtures of methanol, acetone, and chloroform at temperatures from (298.15-318.15) K and ambient pressure
ρl	1469.61	kg/m3	303.15	Temperature Dependence of Densities and Excess Molar Volumes of the Ternary Mixture (1-Butanol + Chloroform + Benzene) and its Binary Constituents (1-Butanol + Chloroform and 1-Butanol + Benzene)
ρl	1470.50	kg/m3	303.15	Viscosity and Density for Binary Mixtures of Carbon Tetrachloride + Chloroform, Carbon Tetrachloride + Dichloromethane, and Chloroform + Dichloromethane and One Ternary Mixture of Chloroform + 1:1 (Carbon Tetrachloride + Dichloromethane) at 303.15 K
ρl	1469.69	kg/m3	303.15	Excess volumes, Viscosities, and Excess Gibbs Energy of Activation for Viscous Flow, for binary and ternary mixtures 1- propanol + N-N dimethylformamid + chloroform at different temperatures
ρl	1469.61	kg/m3	303.15	Densities and Excess Molar Volumes of the Ternary Mixture 2-Butanol + Chloroform + Benzene and Binary Mixtures 2-Butanol + Chloroform, or + Benzene over the Temperature Range (288.15 to 313.15) K
ρl	1469.61	kg/m3	303.15	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
ρl	1469.61	kg/m3	303.15	Volumetric properties of the ternary system ethanol + chloroform + benzene at temperature range (288.15 313.15) K: Experimental data, correlation and prediction by cubic EOS
ρl	1469.63	kg/m3	303.15	Volumetric behaviour of binary mixtures of (trichloromethane + amines) at temperatures between T = (288.15 and 303.15) K at p = 0.1 MPa
ρl	1470.80	kg/m3	308.00	Thermo-physical properties of 1,3,4-oxadiazole derivatives in pure solvents
ρl	1470.80	kg/m3	308.00	Thermo-acoustical studies of 1,3,4-oxadiazole as binary mixture at three different temperatures
ρl	1459.00	kg/m3	308.15	Speed of sound, density and related thermodynamic excess properties of binary mixtures of butan-2-one with C1-C4 nalkanols and chloroform
ρl	1454.33	kg/m3	308.15	Volumetric Study for the Binary Nitromethane with Chloroalkane Mixtures at Temperatures in the Range (298.15 to 318.15) K
ρl	1460.03	kg/m3	308.15	Temperature Dependence of Densities and Excess Molar Volumes of the Ternary Mixture (1-Butanol + Chloroform + Benzene) and its Binary Constituents (1-Butanol + Chloroform and 1-Butanol + Benzene)
ρl	1454.33	kg/m3	308.15	Densities and Excess Molar Volumes of the Binary Mixtures of Cyclopentanone with Chloroalkanes at T = (288.15, 298.15, 308.15, and 318.15) K
ρl	1454.07	kg/m3	308.15	Densities and Excess Molar Volumes of the Binary Mixtures of Cyclohexanone with Chloroalkanes at Temperatures between (288.15 and 318.15) K
ρl	1460.03	kg/m3	308.15	Densities and Excess Molar Volumes of the Ternary Mixture 2-Butanol + Chloroform + Benzene and Binary Mixtures 2-Butanol + Chloroform, or + Benzene over the Temperature Range (288.15 to 313.15) K
ρl	1460.03	kg/m3	308.15	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
ρl	1460.01	kg/m3	308.15	Densities, viscosities, and refractive indices of binary and ternary mixtures of methanol, acetone, and chloroform at temperatures from (298.15-318.15) K and ambient pressure
ρl	1460.03	kg/m3	308.15	Volumetric properties of the ternary system ethanol + chloroform + benzene at temperature range (288.15 313.15) K: Experimental data, correlation and prediction by cubic EOS
ρl	1465.80	kg/m3	313.00	Thermo-physical properties of 1,3,4-oxadiazole derivatives in pure solvents
ρl	1465.80	kg/m3	313.00	Thermo-acoustical studies of 1,3,4-oxadiazole as binary mixture at three different temperatures
ρl	1450.41	kg/m3	313.15	Densities and Excess Molar Volumes of the Ternary Mixture 2-Butanol + Chloroform + Benzene and Binary Mixtures 2-Butanol + Chloroform, or + Benzene over the Temperature Range (288.15 to 313.15) K
ρl	1450.39	kg/m3	313.15	Excess volumes, Viscosities, and Excess Gibbs Energy of Activation for Viscous Flow, for binary and ternary mixtures 1- propanol + N-N dimethylformamid + chloroform at different temperatures
ρl	1450.41	kg/m3	313.15	Volumetric properties of the ternary system ethanol + chloroform + benzene at temperature range (288.15 313.15) K: Experimental data, correlation and prediction by cubic EOS
ρl	1450.39	kg/m3	313.15	Densities, viscosities, and refractive indices of binary and ternary mixtures of methanol, acetone, and chloroform at temperatures from (298.15-318.15) K and ambient pressure
ρl	1450.41	kg/m3	313.15	Temperature Dependence of Densities and Excess Molar Volumes of the Ternary Mixture (1-Butanol + Chloroform + Benzene) and its Binary Constituents (1-Butanol + Chloroform and 1-Butanol + Benzene)
ρl	1450.41	kg/m3	313.15	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
ρl	1440.03	kg/m3	318.15	Densities, viscosities, and refractive indices of binary and ternary mixtures of methanol, acetone, and chloroform at temperatures from (298.15-318.15) K and ambient pressure
ρl	1434.72	kg/m3	318.15	Densities and Excess Molar Volumes of the Binary Mixtures of Cyclohexanone with Chloroalkanes at Temperatures between (288.15 and 318.15) K
ρl	1434.98	kg/m3	318.15	Volumetric Study for the Binary Nitromethane with Chloroalkane Mixtures at Temperatures in the Range (298.15 to 318.15) K
ρl	1434.97	kg/m3	318.15	Densities and Excess Molar Volumes of the Binary Mixtures of Cyclopentanone with Chloroalkanes at T = (288.15, 298.15, 308.15, and 318.15) K
ρl	1429.89	kg/m3	323.15	Excess volumes, Viscosities, and Excess Gibbs Energy of Activation for Viscous Flow, for binary and ternary mixtures 1- propanol + N-N dimethylformamid + chloroform at different temperatures
csound,fluid	[916.63; 984.42]	m/s	[298.15; 318.15]
csound,fluid	984.42	m/s	298.15	Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
csound,fluid	950.45	m/s	308.15	Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
csound,fluid	916.63	m/s	318.15	Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
γ	[0.03; 0.03]	N/m	[293.15; 298.20]
γ	0.03	N/m	293.15	Investigation of Surface Properties and Solubility of 1-Vinyl-3-alkyl/Esterimidazolium Halide Ionic Liquids by Density Functional Methods
γ	0.03	N/m	298.15	NCMS SOLV-DB
γ	0.03	N/m	298.20	KDB

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboil(P)	334.25	K	96.60	Low cost apparatus for rapid boiling point determination of small air sensitive samples under inert atmosphere

Datasets

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
303.15	101.30	0.0005
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
303.15	101.30	0.0005
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[40.38; 100.57]	J/mol×K	[100.00; 1500.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K
Coefficient A			3.66590e+01
Coefficient B			-3.08100e+02
Coefficient C			4.39124e+00
Coefficient D			3.13700e-05
Coefficient E			-3.35380e-08
Temperature range, min.			100.00
Temperature range, max.			1500.00
Cp,gas	40.38	J/mol×K	100.00	Calculated Property
Cp,gas	60.98	J/mol×K	255.56	Calculated Property
Cp,gas	75.10	J/mol×K	411.11	Calculated Property
Cp,gas	83.87	J/mol×K	566.67	Calculated Property
Cp,gas	89.63	J/mol×K	722.22	Calculated Property
Cp,gas	93.60	J/mol×K	877.78	Calculated Property
Cp,gas	96.38	J/mol×K	1033.33	Calculated Property
Cp,gas	98.34	J/mol×K	1188.89	Calculated Property
Cp,gas	99.69	J/mol×K	1344.44	Calculated Property
Cp,gas	100.57	J/mol×K	1500.00	Calculated Property
Cp,gas	[65.33; 98.35]	J/mol×K	[298.00; 1200.00]	NIST
Equation			Y = A + B·t + C·t² + D·t³ + E/t², t = T/1000 Y is Cp,gas in J/mol×K, T in K
Coefficient A			4.42471e+01
Coefficient B			1.14673e+02
Coefficient C			-8.88184e+01
Coefficient D			2.58999e+01
Coefficient E			-5.22808e-01
Reference			Chase, 1998
Comment			F=-122.4891, G=315.7451, H=-103.1770; Data last reviewed in December, 1968
Temperature range, min.			298.00
Temperature range, max.			1200.00
Cp,gas	65.33	J/mol×K	298.00	Calculated Property
Cp,gas	74.17	J/mol×K	398.22	Calculated Property
Cp,gas	80.44	J/mol×K	498.44	Calculated Property
Cp,gas	85.16	J/mol×K	598.67	Calculated Property
Cp,gas	88.78	J/mol×K	698.89	Calculated Property
Cp,gas	91.56	J/mol×K	799.11	Calculated Property
Cp,gas	93.73	J/mol×K	899.33	Calculated Property
Cp,gas	95.47	J/mol×K	999.56	Calculated Property
Cp,gas	96.96	J/mol×K	1099.78	Calculated Property
Cp,gas	98.35	J/mol×K	1200.00	Calculated Property
Cp,gas	[98.23; 107.57]	J/mol×K	[1200.00; 6000.00]	NIST
Equation			Y = A + B·t + C·t² + D·t³ + E/t², t = T/1000 Y is Cp,gas in J/mol×K, T in K
Coefficient A			1.01476e+02
Coefficient B			3.42976e+00
Coefficient C			-6.57348e-01
Coefficient D			4.37070e-02
Coefficient E			-9.34802e+00
Reference			Chase, 1998
Comment			F=-155.8000, G=387.1556, H=-103.1770; Data last reviewed in December, 1968
Temperature range, min.			1200.00
Temperature range, max.			6000.00
Cp,gas	98.23	J/mol×K	1200.00	Calculated Property
Cp,gas	102.56	J/mol×K	1733.33	Calculated Property
Cp,gas	104.56	J/mol×K	2266.67	Calculated Property
Cp,gas	105.69	J/mol×K	2800.00	Calculated Property
Cp,gas	106.38	J/mol×K	3333.33	Calculated Property
Cp,gas	106.81	J/mol×K	3866.67	Calculated Property
Cp,gas	107.08	J/mol×K	4400.00	Calculated Property
Cp,gas	107.26	J/mol×K	4933.33	Calculated Property
Cp,gas	107.41	J/mol×K	5466.67	Calculated Property
Cp,gas	107.57	J/mol×K	6000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[109.41; 121.83]	J/mol×K	[233.15; 366.48]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K
Coefficient A			9.31320e+01
Coefficient B			6.45440e+02
Coefficient C			-4.53386e+00
Coefficient D			2.44570e-02
Coefficient E			-2.10970e-05
Temperature range, min.			233.15
Temperature range, max.			366.48
Cp,liquid	109.41	J/mol×K	233.15	Calculated Property
Cp,liquid	110.19	J/mol×K	247.96	Calculated Property
Cp,liquid	111.17	J/mol×K	262.78	Calculated Property
Cp,liquid	112.33	J/mol×K	277.59	Calculated Property
Cp,liquid	113.64	J/mol×K	292.41	Calculated Property
Cp,liquid	115.10	J/mol×K	307.22	Calculated Property
Cp,liquid	116.67	J/mol×K	322.04	Calculated Property
Cp,liquid	118.33	J/mol×K	336.85	Calculated Property
Cp,liquid	120.06	J/mol×K	351.67	Calculated Property
Cp,liquid	121.83	J/mol×K	366.48	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0019739; 0.0002094]	Pa×s	[209.63; 436.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-2.09230e+01
Coefficient B			1.24890e+03
Coefficient C			1.65500e+00
Coefficient D			-2.47870e-06
Coefficient E			2.00000e+00
Temperature range, min.			209.63
Temperature range, max.			436.00
η	0.0019739	Pa×s	209.63	Calculated Property
η	0.0012234	Pa×s	234.78	Calculated Property
η	0.0008390	Pa×s	259.93	Calculated Property
η	0.0006184	Pa×s	285.09	Calculated Property
η	0.0004805	Pa×s	310.24	Calculated Property
η	0.0003883	Pa×s	335.39	Calculated Property
η	0.0003232	Pa×s	360.54	Calculated Property
η	0.0002752	Pa×s	385.70	Calculated Property
η	0.0002384	Pa×s	410.85	Calculated Property
η	0.0002094	Pa×s	436.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[36.66; 1.50]	kJ/mol	[209.63; 536.40]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K
Coefficient A			5.13820e+01
Coefficient B			7.02700e-01
Coefficient C			3.67480e-01
Coefficient D			-1.35100e+00
Coefficient E			6.92360e-01
Critical temperature, Tc (K)			5.36500e+02
Temperature range, min.			209.63
Temperature range, max.			536.40
ΔvapH	36.66	kJ/mol	209.63	Calculated Property
ΔvapH	34.41	kJ/mol	245.94	Calculated Property
ΔvapH	32.27	kJ/mol	282.25	Calculated Property
ΔvapH	30.21	kJ/mol	318.55	Calculated Property
ΔvapH	28.17	kJ/mol	354.86	Calculated Property
ΔvapH	26.03	kJ/mol	391.17	Calculated Property
ΔvapH	23.61	kJ/mol	427.48	Calculated Property
ΔvapH	20.57	kJ/mol	463.78	Calculated Property
ΔvapH	16.07	kJ/mol	500.09	Calculated Property
ΔvapH	1.50	kJ/mol	536.40	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 5482.48]	kPa	[244.65; 536.40]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.43630e+01
Coefficient B			-2.83926e+03
Coefficient C			-4.29370e+01
Temperature range, min.			244.65
Temperature range, max.			536.40
Pvap	1.33	kPa	244.65	Calculated Property
Pvap	9.36	kPa	277.07	Calculated Property
Pvap	40.90	kPa	309.48	Calculated Property
Pvap	129.81	kPa	341.90	Calculated Property
Pvap	328.67	kPa	374.32	Calculated Property
Pvap	705.23	kPa	406.73	Calculated Property
Pvap	1335.51	kPa	439.15	Calculated Property
Pvap	2296.22	kPa	471.57	Calculated Property
Pvap	3658.33	kPa	503.98	Calculated Property
Pvap	5482.48	kPa	536.40	Calculated Property
Pvap	[0.05; 5500.00]	kPa	[207.15; 532.56]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K
Coefficient A			9.30074e+01
Coefficient B			-6.78156e+03
Coefficient C			-1.19387e+01
Coefficient D			1.15883e-05
Coefficient E			2.00000e+00
Comment			Range stopped where the equation exceeds Pc; ChemSep gives it to 536.4 K.
Temperature range, min.			207.15
Temperature range, max.			532.56
Pvap	0.05	kPa	207.15	Calculated Property
Pvap	1.25	kPa	243.31	Calculated Property
Pvap	10.99	kPa	279.46	Calculated Property
Pvap	53.17	kPa	315.62	Calculated Property
Pvap	175.33	kPa	351.78	Calculated Property
Pvap	448.25	kPa	387.94	Calculated Property
Pvap	964.96	kPa	424.09	Calculated Property
Pvap	1848.38	kPa	460.25	Calculated Property
Pvap	3272.28	kPa	496.41	Calculated Property
Pvap	5500.00	kPa	532.56	Calculated Property
Pvap	[0.08; 5628.11]	kPa	[209.63; 536.40]	KDB Vapor Pressure Data
Equation			ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K
Coefficient A			8.11439e+01
Coefficient B			-6.35114e+03
Coefficient C			-1.00709e+01
Coefficient D			9.12761e-06
Coefficient E			0.00000e+00
Temperature range, min.			209.63
Temperature range, max.			536.40
Pvap	0.08	kPa	209.63	Calculated Property
Pvap	1.54	kPa	245.94	Calculated Property
Pvap	12.69	kPa	282.25	Calculated Property
Pvap	59.51	kPa	318.55	Calculated Property
Pvap	192.92	kPa	354.86	Calculated Property
Pvap	487.71	kPa	391.17	Calculated Property
Pvap	1039.15	kPa	427.48	Calculated Property
Pvap	1965.80	kPa	463.78	Calculated Property
Pvap	3422.90	kPa	500.09	Calculated Property
Pvap	5628.11	kPa	536.40	Calculated Property
Pvap	[0.13; 101.27]	kPa	[215.00; 334.40]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.42938e+01
Coefficient B			-2.83938e+03
Coefficient C			-4.09530e+01
Reference			Stull, 1947
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			215.00
Temperature range, max.			334.40
Pvap	0.13	kPa	215.00	Calculated Property
Pvap	0.42	kPa	228.27	Calculated Property
Pvap	1.15	kPa	241.53	Calculated Property
Pvap	2.76	kPa	254.80	Calculated Property
Pvap	6.00	kPa	268.07	Calculated Property
Pvap	11.96	kPa	281.33	Calculated Property
Pvap	22.19	kPa	294.60	Calculated Property
Pvap	38.70	kPa	307.87	Calculated Property
Pvap	64.05	kPa	321.13	Calculated Property
Pvap	101.27	kPa	334.40	Calculated Property
Pvap	[101.69; 5040.38]	kPa	[334.40; 527.00]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.51278e+01
Coefficient B			-3.42269e+03
Coefficient C			-8.61200e+00
Reference			Stull, 1947
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			334.40
Temperature range, max.			527.00
Pvap	101.69	kPa	334.40	Calculated Property
Pvap	194.32	kPa	355.80	Calculated Property
Pvap	344.42	kPa	377.20	Calculated Property
Pvap	573.30	kPa	398.60	Calculated Property
Pvap	905.01	kPa	420.00	Calculated Property
Pvap	1365.58	kPa	441.40	Calculated Property
Pvap	1982.19	kPa	462.80	Calculated Property
Pvap	2782.34	kPa	484.20	Calculated Property
Pvap	3793.09	kPa	505.60	Calculated Property
Pvap	5040.38	kPa	527.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[1627.88; 557.17]	kg/m3	[209.00; 535.95]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K
Coefficient A			6.39339e+01
Coefficient B			1.84040e-01
Coefficient C			5.36500e+02
Coefficient D			1.85410e-01
Temperature range, min.			209.00
Temperature range, max.			535.95
ρl	1627.88	kg/m3	209.00	Calculated Property
ρl	1574.55	kg/m3	245.33	Calculated Property
ρl	1517.54	kg/m3	281.66	Calculated Property
ρl	1455.92	kg/m3	317.98	Calculated Property
ρl	1388.38	kg/m3	354.31	Calculated Property
ρl	1312.82	kg/m3	390.64	Calculated Property
ρl	1225.58	kg/m3	426.97	Calculated Property
ρl	1119.25	kg/m3	463.29	Calculated Property
ρl	973.35	kg/m3	499.62	Calculated Property
ρl	557.17	kg/m3	535.95	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 0.02]	N/m	[209.55; 334.25]	Jasper (1972), surface tension of pure liquid compounds Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is γ in N/m, T in K
Coefficient A			6.52829e-02
Coefficient B			-1.29500e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			209.55
Temperature range, max.			334.25
γ	0.04	N/m	209.55	Calculated Property
γ	0.04	N/m	223.41	Calculated Property
γ	0.03	N/m	237.26	Calculated Property
γ	0.03	N/m	251.12	Calculated Property
γ	0.03	N/m	264.97	Calculated Property
γ	0.03	N/m	278.83	Calculated Property
γ	0.03	N/m	292.68	Calculated Property
γ	0.03	N/m	306.54	Calculated Property
γ	0.02	N/m	320.39	Calculated Property
γ	0.02	N/m	334.25	Calculated Property
γ	[0.04; 1.52e-05]	N/m	[209.63; 534.44]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K
Coefficient A			-1.28050e-02
Coefficient B			8.04960e+01
Coefficient C			-3.47860e+00
Coefficient D			2.25590e-03
Coefficient E			-7.82280e-06
Comment			Range stopped where the equation turns negative; ChemSep gives it to 536.4 K.
Temperature range, min.			209.63
Temperature range, max.			534.44
γ	0.04	N/m	209.63	Calculated Property
γ	0.03	N/m	245.72	Calculated Property
γ	0.03	N/m	281.81	Calculated Property
γ	0.02	N/m	317.90	Calculated Property
γ	0.02	N/m	353.99	Calculated Property
γ	0.01	N/m	390.08	Calculated Property
γ	0.01	N/m	426.17	Calculated Property
γ	0.01	N/m	462.26	Calculated Property
γ	0.00	N/m	498.35	Calculated Property
γ	1.52e-05	N/m	534.44	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.00; 0.05]	W/m×K	[209.63; 1000.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K
Coefficient A			4.11670e-04
Coefficient B			8.44760e-01
Coefficient C			1.87060e+03
Coefficient D			-7.82950e+03
Temperature range, min.			209.63
Temperature range, max.			1000.00
λgas	0.00	W/m×K	209.63	Calculated Property
λgas	0.01	W/m×K	297.45	Calculated Property
λgas	0.01	W/m×K	385.27	Calculated Property
λgas	0.02	W/m×K	473.09	Calculated Property
λgas	0.02	W/m×K	560.91	Calculated Property
λgas	0.03	W/m×K	648.72	Calculated Property
λgas	0.03	W/m×K	736.54	Calculated Property
λgas	0.04	W/m×K	824.36	Calculated Property
λgas	0.04	W/m×K	912.18	Calculated Property
λgas	0.05	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.14; 0.10]	W/m×K	[209.63; 400.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is λliquid in W/m×K, T in K
Coefficient A			6.14170e-02
Coefficient B			-6.66920e+01
Coefficient C			-1.68020e+00
Coefficient D			-1.96200e-03
Coefficient E			-4.41920e-06
Temperature range, min.			209.63
Temperature range, max.			400.00
λliquid	0.14	W/m×K	209.63	Calculated Property
λliquid	0.13	W/m×K	230.78	Calculated Property
λliquid	0.13	W/m×K	251.93	Calculated Property
λliquid	0.12	W/m×K	273.09	Calculated Property
λliquid	0.12	W/m×K	294.24	Calculated Property
λliquid	0.11	W/m×K	315.39	Calculated Property
λliquid	0.11	W/m×K	336.54	Calculated Property
λliquid	0.10	W/m×K	357.70	Calculated Property
λliquid	0.10	W/m×K	378.85	Calculated Property
λliquid	0.10	W/m×K	400.00	Calculated Property

Similar Compounds

Find more compounds similar to Trichloromethane.

Mixtures

• Trichloromethane + Acetonitrile
• Trichloromethane + Acetonitrile + Ethanol
• Benzene + Trichloromethane + Acetone
• Benzene + Trichloromethane + Acetone + Methyl Alcohol
• Trichloromethane + Acetone
• n-Hexane + Trichloromethane + Acetone
• Trichloromethane + Acetone + Methyl Alcohol
• Trichloromethane + Acetone + Water
• Trichloromethane + Ethanol + Acetone
• n-Hexane + Trichloromethane + Ethanol + Acetone
• Trichloromethane + Ethanol + Acetone + Methyl Alcohol
• Trichloromethane + Acetone + Ethyl Acetate
• Benzene + Trichloromethane + Ethanol
• Trichloromethane + Ethanol
• n-Hexane + Trichloromethane + Ethanol
• Trichloromethane + Ethanol + Methyl Alcohol
• Trichloromethane + Ethanol + Water
• Trichloromethane + Ethyl ether
• Trichloromethane + Ethyl Acetate
• Trichloromethane + Ethyl Acetate + Methyl Alcohol

Find more mixtures with Trichloromethane.

Sources

• KDB Vapor Pressure Data
• Active Thermochemical Tables 1.112, gas-phase enthalpies of formation ChEDL chemicals 1.5.2, from Active Thermochemical Tables (ATcT), version 1.112, Argonne National Laboratory; Ruscic, B. et al. Active Thermochemical Tables: Thermochemistry for the 21st Century. J. Phys.: Conf. Ser. 2005, 16, 561.
• Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
• IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 10 ChEDL chemicals 1.5.2, from Marsh, K. N.; Abramson, A.; Ambrose, D.; Morton, D. W.; Nikitin, E.; Tsonopoulos, C.; Young, C. L. Vapor-Liquid Critical Properties of Elements and Compounds. 10. Organic Compounds Containing Halogens. J. Chem. Eng. Data 2007, 52, 1509-1538.
• Jasper (1972), surface tension of pure liquid compounds ChEDL chemicals 1.5.2, from Jasper, J. J. The Surface Tension of Pure Liquid Compounds. J. Phys. Chem. Ref. Data 1972, 1, 841-1010 (as transcribed in Lange's Handbook).
• PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
• Staveley, Lobo and Calado (1981), triple points ChEDL chemicals 1.5.2, from Staveley, L. A. K.; Lobo, L. Q.; Calado, J. C. G. Triple-Points of Low Melting Substances and Their Use in Cryogenic Work. Cryogenics 1981, 21, 131-144.
• ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
• Dortmund Data Bank Vapor-Liquid Equilibrium Data
• Temperature Dependence of Densities and Excess Molar Volumes of the Ternary Mixture (1-Butanol + Chloroform + Benzene) and its Binary Constituents (1-Butanol + Chloroform and 1-Butanol + Benzene)
• Isobaric vapour liquid equilibria for binary mixtures of 1,2-dibromoethane with 1,2-dichloroethane, trichloromethane, and 1,1,2,2-tetrachloroethane at atmospheric pressure
• Liquid liquid equilibria for the system (water + carboxylic acid + chloroform): Thermodynamic modeling
• Volumetric properties of the ternary system ethanol + chloroform + benzene at temperature range (288.15 313.15) K: Experimental data, correlation and prediction by cubic EOS
• Solubility of naproxen in several organic solvents at different temperatures
• Hydrogen substitution effect on the solubility of perhalogenated compounds in ionic liquid [bmim][PF6]
• 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 pressure and excess Gibbs energy of binary 1,2-dichloroethane + cyclohexanone, chloroform + cyclopentanone and chloroform + cyclohexanone mixtures at temperatures from 298.15 to 318.15 K
• Experimental measurements and correlations of vapor liquid equilibrium data for the binary system of chloroform +N,N-dimethylformamide at 101.3 kPa
• Determination of vapour-liquid and vapour-liquid-liquid equilibrium of the chloroform-water and trichloroethylene-water binary mixtures
• Excess Gibbs energies and volumes of the ternary system chloroform + tetrahydrofuran + cyclohexane at 298.15 K
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
• Thermodynamics of the solubility of lomefloxacin in methanol, ethanol, 1-propanol, 2-propanol, acetone, and chloroform from 293.15 to 323.15 K
• Activity coefficients at infinite dilution of organic solutes in 1-octyl-3-methylimidazolium nitrate using gas-liquid chromatography
• The choice of solvent and liquid liquid equilibrium for ternary water + 2-methylaziridine + chloroform system: Experimental data and modeling
• Solubility of 1, 3, 2-dioxaphosphorinane-5,5-dimethyl -2- (2,4,6-tribromophenoxy)-2-oxide in selected solvents
• Solubility and solution thermodynamics of 2,3,4,5-tetrabromothiophene in (ethanol + trichloromethane) binary solvent mixtures
• Thermostabilities and solubilities of flame retardant bisphenol S-bis (5,5-dimethyl-1,3-dioxaphosphorinanyl-2-oxy phosphate ester) as a function of temperature
• Experimental and theoretical study of interaction between organic compounds and 1- (4-sulfobutyl)-3-methylimidazolium based ionic liquids
• Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
• Study of interaction between organic compounds and mono or dicationic oxygenated ionic liquids using gas chromatography
• The role of organic diluents in the aspects of equilibrium, kinetics and thermodynamic model for silver ion extraction using an extractant D2EHPA
• Solid-liquid equilibrium of diphenyl anilinophosphonate in the different organic solvents
• Measurement and correlation of solid-liquid equilibria for three binaries, ethanol-antipyrine, chloroform-antipyrine, and dimethyl ether-antipyrine
• Liquid-liquid equilibria and COSMO-SAC modeling of organic solvent/ ionic liquid - hydroxyacetone - water mixtures
• Isobaric vapor-liquid equilibrium for chloroform + isopropanol + 1,3-dimethylimidazolium dimethylphosphate at 101.3 kPa
• Isobaric vapor-liquid equilibrium for chloroform + ethanol + 1,3- dimethylimidazolium dimethylphosphate at 101.3 kPa
• Densities, viscosities, and refractive indices of binary and ternary mixtures of methanol, acetone, and chloroform at temperatures from (298.15-318.15) K and ambient pressure
• Measurements of activity coefficients at infinite dilution for organic solutes in two quaternary ammonium-based ionic liquids [DDA][ClO4] and [DDA][BF4]
• 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
• Thermochemical study of two anhydrous polymorphs of caffeine
• Density, viscosity, isothermal (vapour + liquid) equilibrium, excess molar volume, viscosity deviation, and their correlations for chloroform + methyl isobutyl ketone binary system
• Measurement of activity coefficients at infinite dilution in 1-hexadecyl-3-methylimidazolium tetrafluoroborate ionic liquid
• Phase diagrams of (vapour + liquid) equilibrium for binary mixtures of a,a,a-trifluorotoluene with ethanol, or benzene, or chloroform at pressure 101.4 kPa
• Volumetric behaviour of binary mixtures of (trichloromethane + amines) at temperatures between T = (288.15 and 303.15) K at p = 0.1 MPa
• Thermodynamic properties of solvation of aromatic compounds in cyclohexane, heptane, benzene, 1,4-dioxane, and chloroform at 298.15 K
• Enthalpies of solvation of ethylene oxide oligomers CH3O(CH2CH2O)nCH3 (n = 1 to 4) in different H-bonding solvents: Methanol, chloroform, and water. Group contribution method as applied to the polar oligomers
• Interactions of volatile organic compounds with the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
• 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
• Henry s constants and activity coefficients of some organic solutes in 1-butyl,3-methylimidazolium hydrogen sulfate and in 1-methyl,3-trimethylsilylmethylimidazolium chloride
• Thermo-physical properties of 1,3,4-oxadiazole derivatives in pure solvents
• Interactions of volatile organic compounds with the ionic liquids 1-butyl-1-methylpyrrolidinium tetracyanoborate and 1-butyl-1-methylpyrrolidinium bis(oxalato)borate
• Solubilities of evodiamine in twelve organic solvents from T = (283.2 to 323.2) K
• Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds Part II: C18 fatty acids
• Infinite dilution activity coefficients of volatile organic compounds in two ionic liquids composed of the tris(pentafluoroethyl) trifluorophosphate ([FAP]) anion and a functionalized cation
• Thermo-acoustical studies of 1,3,4-oxadiazole as binary mixture at three different temperatures
• 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
• Measurement, correlation and dissolution thermodynamics of biological active chalcone in organic solvents at different temperatures
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-butyl-3-methylimidazolium methyl sulfate
• Blood porphyrins in binary mixtures of N,N-dimethylformamide with 1-octanol and chloroform: The energetics of solvation, (solute + cosolvent) interactions and model calculations
• Activity coefficients at infinite dilution of organic solutes in methylphosphonate based ionic liquids using gas-liquid chromatography
• Solubility of daidzin in different organic solvents and (ethyl alcohol + water) mixed solvents
• Measurement and correlation of the solubility of genistin in eleven organic solvents from T = (283.2 to 323.2) K
• 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
• Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-hexyl-2,3-dimethylimidazolium bis(trifluoromethylsulfonyl)imide
• Thermodynamic modelling for solubility of 5-chloro-1-methyl-4-nitroimidazole in eleven organic solvents from T = (283.15 to 318.15) K
• Thermodynamic study of solubility for 2-amino-4-chloro-6-methoxypyrimidine in twelve organic solvents at temperatures from 273.15 K to 323.15 K
• Determination and correlation of solubility of 11alpha,17alpha-dihydroxy-4-pregnene-3,20-dione in different solvents
• 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
• Thermodynamics and activity coefficients at infinite dilution for organic compounds and water in the ionic liquid 1-butyl-3-methylimidazolium perchlorate
• Separation of azeotrope (2,2,3,3-tetrafluoro-1-propanol + water): Isobaric vapour-liquid phase equilibrium measurements and azeotropic distillation
• Separation of binary mixtures based on gamma infinity data using [OMMIM][NTf2] ionic liquid and modelling of thermodynamic functions
• Abraham model correlations for describing the thermodynamic properties of solute transfer into pentyl acetate based on headspace chromatographic and solubility measurements
• Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in ionic liquid [HMMIM][BF4]
• Thermodynamics and activity coefficients at infinite dilution for organic compounds in the ionic liquid 1-hexyl-3-methylimidazolium chloride
• Separation of binary mixtures based on gamma infinity data using [OMMIM][BF4] ionic liquid and modelling of thermodynamic functions
• Determination of the thermodynamic parameters of ionic liquid 1-propyl-3-methylimidazolium bromide by gas-liquid chromatography
• Liquid-liquid equilibrium study for ternary systems of water + propargyl alcohol + solvents at 308.2 K: Measurement and thermodynamic modelling
• Speeds of sound, isentropic compressibilities, viscosities, and excess molar volumes of binary mixtures of alkanoates with tetra- and trichloromethanes at 303.15 K
• Densities, speeds of sound, isentropic compressibilities, refractive indexes, and viscosities of tetrahydrofuran with haloalkane or alkyl ethanoate at T = 303.15 K
• Studies of viscosities of dilute solutions of alkylamine in non-electrolyte solvents. II. Haloalkanes and other polar solvents
• Topological and thermodynamic investigations of molecular interactions of aniline and o-toluidine with chloroform
• Effect of electrostatic interaction on thermochemical behavior of 12-crown-4 ether in various polar solvents
• Excess volumes, Viscosities, and Excess Gibbs Energy of Activation for Viscous Flow, for binary and ternary mixtures 1- propanol + N-N dimethylformamid + chloroform at different temperatures
• Effect of halogen substitution on the enthalpies of solvation and hydrogen bonding of organic solutes in chlorobenzene and 1,2-dichlorobenzene derived using multi-parameter correlations
• Thermodynamics of hydrogen bonding and van der Waals interactions of organic solutes in solutions of imidazolium based ionic liquids: "structure-property" relationships
• Enthalpies of solution of 1-ethyl- and 1-butyl-3-methylimidazolium based ionic liquids in tetrahydrofuran and chloroform at 298.15 K: Thermochemical proton acceptor scale of anions
• Low cost apparatus for rapid boiling point determination of small air sensitive samples under inert atmosphere
• Solubilities of Phosphoramidic Acid, N-(phenylmethyl)-, Diphenyl Ester in Selected Solvents
• Dissociation Constants and Solubilities of Dalbergin and Nordalbergin in Different Solvents
• Investigation of Surface and Solubility Properties of N-Vinylimidazolium Tetrahalogenidoferrate(III) Magnetic Ionic Liquids Using Density Functional Theory
• Comparing Composition- and Temperature-Dependent Viscosities of Binary Systems Involving Ionic Liquids
• Measurement and Correlation of the Solubility for Camptothecine in Different Organic Solvents
• Solubility Measurement and Thermodynamic Modeling of 4-Nitrophthalimide in Twelve Pure Solvents at Elevated Temperatures Ranging from (273.15 to 323.15) K
• Solubility Measurement and Correlation for e-2,4,6,8,10,12-Hexanitro-2,4,6,8,10,12-hexaazaisowurtzitane in Five Organic Solvents at Temperatures between 283.15 and 333.15 K and Different Chloralkane + Ethyl Acetate Binary Solvents at Temperatures between 283.15 and 323.15 K
• Measurement and Correlation of the Solubility of e-CL-20 in 12 Organic Solvents at Temperatures Ranging from 278.15 to 318.15 K
• Measurements and Thermodynamic Models for the Separation of 2-Methoxyethanol and Water Azeotropic Mixtures via Different Solvents
• Measurement and Thermodynamic Modeling of Ternary (Liquid + Liquid) Equilibrium for Extraction of N,N-Dimethylacetamide from Aqueous Solution with Different Solvents
• Solid Liquid Phase Equilibrium of N,N'-Piperazinebis(neopentylglycol)phosphoramidate in Selected Solvents from T = (293.15 to 333.15) K
• Determination of Infinite Dilution Activity Coefficients of Several Organic Solutes in N-Butylpyridinium Nitrate/N-Octylpyridinium Nitrate by Blend Inverse Gas Chromatography
• 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
• 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
• 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
• Determination and Thermodynamic Analysis of the Solubility of Limonin in Eight Organic Solvents and Ethyl Acetate + 2-Propanol Binary Solvents from 283.2 to 323.2 K
• Solubility Measurement and Thermodynamic Modeling of Benzoic Acid in Monosolvents and Binary Mixtures
• Determination of Activity Coefficients at Infinite Dilution of Organic Solutes in the Ionic Liquid 1-(2-Hydroxyethyl)-3-methylimidazolium Nonafluoro-1-butanesulfonate Using Gas-Liquid Chromatography
• Solubilities of Organic Semiconductors and Nonsteroidal Anti-inflammatory Drugs in Pure and Mixed Organic Solvents: Measurement and Modeling with Hansen Solubility Parameter
• Determination of Activity Coefficients at Infinite Dilution of Solutes in N,N'-Di(2-ethylhexyl)isobutyramide Using Inverse Gas-Liquid Chromatography
• Isobaric Vapor-Liquid Phase Equilibrium Measurements for Allyl Alcohol with Chloroform, Ethyl Acetate, and Methyl Propionate at 101.3 kPa
• Liquid-Liquid Equilibrium for the Ternary System of 3-Mercaptopropionic Acid + Water + Trichloromethane
• Measurement and Correlation of the Solubility of 2-Cyanoacetamide in 14 Pure Solvents and the Mixing Properties of Solutions
• Equilibrium Solubility, Model Correlation, and Solvent Effect of Indole-3-acetic Acid in Twelve Pure Solvents
• Thermodynamic Studies of Solubility for Naphthalene in 12 Solvents from 279 to 330 K
• Solubility and Thermodynamic Modeling of Dimethyl Terephthalate in Pure Solvents and the Evaluation of the Mixing Properties of the Solutions
• Viscosity and Density for Binary Mixtures of Carbon Tetrachloride + Chloroform, Carbon Tetrachloride + Dichloromethane, and Chloroform + Dichloromethane and One Ternary Mixture of Chloroform + 1:1 (Carbon Tetrachloride + Dichloromethane) at 303.15 K
• Measurement of Activity Coefficients of Solutes at Infinite Dilution in (Dimethyl Sulfoxide + Acetamide, or Formamide, or Urea) Using Gas Liquid Chromatography at the Temperature 298.15 K
• Total Vapor Pressure Measurements for 2-Ethoxyethanol with Carbon Tetrachloride, Chloroform, and Dichloromethane at 303.15 K
• Density, Viscosity, and Excess Properties of Binary Liquid Mixtures of Propylene Carbonate with Polar and Nonpolar Solvents
• Phase Separation in Binary Mixtures Containing Linear Perfluoroalkanes
• Solid-Liquid Equilibria for Benzoic Acid + p-Toluic Acid + Chloroform, Benzoic Acid + p-Toluic Acid + Acetic Acid, and Terephthalic Acid + Isophthalic Acid + N,N-Dimethylformamide
• Densities, Viscosities, and Ultrasonic Velocity Studies of Binary Mixtures of Chloroform with Propan-1-ol and Butan-1-ol at (303.15 and 313.15) K
• 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
• 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
• Densities, Viscosities, and Ultrasonic Velocity Studies of Binary Mixtures of Chloroform with Pentan-1-ol, Hexan-1-ol, and Heptan-1-ol at (303.15 and 313.15) K
• Solubility of Erythromycin A Dihydrate in Different Pure Solvents and Acetone + Water Binary Mixtures between 293 K and 323 K
• Activity Coefficients at Infinite Dilution in 1-Alkyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
• Thermodynamic Properties of Mixtures Containing Ionic Liquids: Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Propyl Boronic Acid-3-Alkylimidazolium Bromide and 1-Propenyl-3-alkylimidazolium Bromide Using Inverse Gas Chromatography
• Density, Viscosity, Vapor-Liquid Equilibrium, Excess Molar Volume, Viscosity Deviation, and Their Correlations for the Chloroform + 2-Butanone Binary System
• Densities, Viscosities, and Ultrasonic Velocity Studies of Binary Mixtures of Chloroform with Octan-1-ol and Decan-1-ol at (303.15 and 313.15) K
• Activity Coefficients at Infinite Dilution of Polar Solutes in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• 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
• Solubility of Physalin D in Ethanol, Methanol, Propanone, Trichloromethane, Ethyl Ethanoate, and Water at Temperatures from (283.2 to 313.2) K
• Solubilities of Phosphorus-Containing Compounds in Selected Solvents
• Partial Molar Volumes of N,N'-1,2-Ethyl-bis(salicyladimine) Schiff Base (Salen) in Organic Solvents at T = (283.15 to 318.15) K
• Activity Coefficients at Infinite Dilution for Hydrocarbons in Fatty Alcohols Determined by Gas-Liquid Chromatography
• Solubility and Crystal Size of Sirolimus in Different Organic Solvents
• Solubility of Benzoic Acid in Pure Solvents and Binary Mixtures
• Liquid-Liquid Equilibrium, Solid-Liquid Equilibrium, Densities, and Refractivity of a Water, Chloroform, and Acetylacetone Mixture
• Solubilities of N-[(4-Bromo-3,5-difluorine)-phenyl]maleimide in Pyridine, Acetone, Tetrahydrofuran, Ethanol, Trichloromethane, and Acetonitrile at Temperature between (285.00 and 350.15) K
• Density, Viscosity, Vapor-Liquid Equilibrium, and Excess Molar Enthalpy of [Chloroform + Methyl tert-Butyl Ether]
• Solubilities of Phenylphosphinic Acid, Methylphenylphosphinic Acid, Hexachlorocyclotriphosphazene, and Hexaphenoxycyclotriphosphazene in Selected Solvents
• Activity Coefficients at Infinite Dilution in Methylimidazolium Nitrate Ionic Liquids
• Measurement and Correlation of the Solubility of Prednisone Acetate in Different Solvents
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Butyl-3-methylimidazolium Nitrate Using Gas-Liquid Chromatography
• Activity Coefficients at Infinite Dilution of Organic Compounds in Four New Imidazolium-Based Ionic Liquids
• Solubilities of Tris(o-phenylenedioxy)cyclotriphosphazene in Selected Solvents
• Partition Coefficients of Organic Compounds in Four New Tetraalkylammonium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Using Inverse Gas Chromatography
• Interactions of Volatile Organic Compounds with the Ionic Liquid 1-Butyl-1-methylpyrrolidinium Dicyanamide
• Evaluation of the Performance of Trigeminal Tricationic Ionic Liquids for Separation Problems
• Solubilities of 3-Methoxy-N-phenylaniline and 3-(Methylthio)-N-phenylaniline in Five Organic Solvents (285 K to 333.75 K)
• Crystal Structures, Reaction Rates, and Selected Physical Properties of Halo-Boronsubphthalocyanines (Halo = Fluoride, Chloride, and Bromide)
• 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
• Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
• Solubilities of 4,4'-Dichlorodiphenyl Disulfide in Six Organic Solvents between (303.15 and 333.15) K
• Volumetric Study for the Binary Nitromethane with Chloroalkane Mixtures at Temperatures in the Range (298.15 to 318.15) K
• Solubilities of 4-Amino-4?-nitrodiphenyl Sulfide in Six Organic Solvents from 287.45 K to 365.55 K
• Solubilities of Rutaecarpine in Twelve Organic Solvents from (283.2 to 323.2) K
• 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
• 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
• Solubility of Benzyl Disulfide in Five Organic Solvents between (283.45 and 333.15) K
• Solubilities of Phosphonic Acid, P,P'-(1,4-Piperazinediyl)bis-,P,P,P',P'-tetraphenyl Ester in Selected 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 1-Fluoro-4-(methylsulfonyl)benzene in Five Pure Organic Solvents at Temperatures from (288.40 to 331.50) K
• Solubilities of 4-(Hydroxymethyl)-1-oxido-2,6,7-trioxa-1-phosphabicyclo[2.2.2]octane in Organic Solvents
• 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
• Infinite Dilution Activity Coefficients of Solutes Dissolved in Two Trihexyl(tetradecyl)phosphonium Ionic Liquids
• Investigation of Surface Properties and Solubility of 1-Vinyl-3-alkyl/Esterimidazolium Halide Ionic Liquids by Density Functional Methods
• Speed of sound, density and related thermodynamic excess properties of binary mixtures of butan-2-one with C1-C4 nalkanols and chloroform
• 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
• 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
• Solubilities of Betulin in Fourteen Organic Solvents at Different Temperatures
• Study of Vapor-Liquid Equilibrium for Binary Mixtures (Chloroform + 2,2,2-Trifluoroethanol) and (r,r,r-Trifluorotoluene + 2,2,2-Trifluoroethanol) at Pressure 102 kPa
• Densities and Excess Molar Volumes of the Binary 1-Propanol + Chloroform and 1-Propanol + Benzene and Ternary 1-Propanol + Chloroform + Benzene Mixtures at (288.15, 293.15, 298.15, 303.15, 308.15, and 313.15) K
• Solubility of Irbesartan (Form A) in Different Solvents between 278 K and 323 K
• Solubility of Imidacloprid in Different Solvents
• Phase Equilibria of Acrylonitrile and p-Bromobenzaldehyde in Carbon Dioxide
• 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
• Activity Coefficients at Infinite Dilution of Polar Solutes in 1-Propyl-2,3-dimethylimidazolium Tetrafluoroborate Using Gas Liquid Chromatography
• Solubility of Rifapentine in Different Organic Solvents
• Densities and Excess Molar Volumes of the Ternary Mixture 2-Butanol + Chloroform + Benzene and Binary Mixtures 2-Butanol + Chloroform, or + Benzene over the Temperature Range (288.15 to 313.15) K
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Ethyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Solubility of Pyoluteorin in Water, Dichloromethane, Chloroform, and Carbon Tetrachloride from (278.2 to 333.2) K
• Solubility of the Antimicrobial Agent Triclosan in Organic Solvents of Different Hydrogen Bonding Capabilities at Several Temperatures
• Solubility of Artemisinin in Seven Different Pure Solvents from (283.15 to 323.15) K
• Isobaric Vapor-Liquid and Liquid-Liquid Equilibria for Chloroform + Ethanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
• Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Inverse Gas Chromatography
• Solubility of Fluorene in Benzene, Chloroform, Acetone, 1-Propanol, Isobutanol, and Methylbenzene from (283 to 323) K
• Solubility of Adipic Acid in Acetone, Chloroform, and Toluene
• Activity Coefficients at Infinite Dilution of Organic Compounds in Trihexyl(tetradecyl)phosphonium Bis(trifluoromethylsulfonyl)imide Using Inverse Gas Chromatography
• Solubility of 2-Aminopyridine in Acetone, Chloroform, and Ethyl Acetate
• Solubility of Valsartan in Different Organic Solvents and Ethanol + Water Binary Mixtures from (278.15 to 313.15) K
• Solubility of Canthaxanthin in Pure Solvents from (293.15 to 343.15) K
• Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
• Densities and Excess Molar Volumes of the Binary Mixtures of Cyclohexanone with Chloroalkanes at Temperatures between (288.15 and 318.15) K
• Solubility of Ofloxacin in 1,2-Dichloromethane, Chloroform, Carbon Tetrachloride, and Water from (293.15 to 313.15) K
• Isobaric Vapor-Liquid and Liquid-Liquid Equilibria for Chloroform + Methanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
• Activity Coefficients at Infinite Dilution of Polar Solutes in 1-(2-Hydroxyethyl)-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Solubilities of Sulfadiazine in Methanol, Ethanol, 1-Propanol, 2-Propanol, Acetone, and Chloroform from (294.15 to 318.15) K
• Study of Ether-, Alcohol-, or Cyano-Functionalized Ionic Liquids Using Inverse Gas Chromatography
• Densities and Excess Molar Volumes of the Binary Mixtures of Cyclopentanone with Chloroalkanes at T = (288.15, 298.15, 308.15, and 318.15) K
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• NCMS SOLV-DB
• The Yaws Handbook of Vapor Pressure
• Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD

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