Chemical Properties of Carbon Tetrachloride (CAS 56-23-5)

InChI

InChI=1S/CCl4/c2-1(3,4)5

InChI Key

VZGDMQKNWNREIO-UHFFFAOYSA-N

Formula

CCl4

SMILES

ClC(Cl)(Cl)Cl

Molecular Weight¹

153.82

CAS

56-23-5

Other Names

• Benzenoform
• Benzinoform
• CCl4
• Carbon chloride (CCl4)
• Carbon tet
• Carbona
• Chlorid uhlicity
• Czterochlorek wegla
• ENT 27164
• ENT 4,705
• Fasciolin
• Flukoids
• Freon 10
• Halon 1040
• Katharin
• Methane tetrachloride
• Methane, tetrachloro-
• NSC 97063
• Necatorina
• Necatorine
• Perchloromethane
• R 10
• R 10 (Refrigerant)
• R-10
• REFRIGERANT-10
• Rcra waste number U211
• Seretin
• Tetrachloorkoolstof
• Tetrachloormetaan
• Tetrachlorkohlenstoff, tetra
• Tetrachlormethan
• Tetrachlorocarbon
• Tetrachlorure de carbone
• Tetraclorometano
• Tetracloruro di carbonio
• Tetrafinol
• Tetraform
• Tetrasol
• Thawpit
• UN 1846
• Univerm
• Vermoestricid
• tetrachloromethane

• ω : Acentric Factor.
• α_p : Isobaric thermal expansion coefficient (1/K).
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• C_p,solid : Solid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• EA : Electron affinity (eV).
• 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_subH : Enthalpy of sublimation 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 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 : Polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• c_sound,fluid : Speed of sound in fluid (m/s).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• λ : Gas thermal conductivity (W/m×K).
• λ : 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).
• 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. Datasets
4. Correlations
5. Similar Compounds
6. Mixtures
7. Sources

Physical Properties

Property	Value	Unit	Source
ω	[0.1870; 0.1930]
ω	0.1870		ChemSep v8.3 pure component data
ω	0.1930		KDB
ΔcH°liquid	[-365.70; -359.90]	kJ/mol
ΔcH°liquid	-359.90	kJ/mol	NIST
ΔcH°liquid	-365.70 ± 8.40	kJ/mol	NIST
μ	[0.00; 0.00]	debye
μ	0.00	debye	ChemSep v8.3 pure component data
μ	0.00	debye	KDB
η	[0.0009020; 0.0009096]	Pa×s
η	0.0009096	Pa×s	Densities and Viscosities of Binary Liquid Mixtures of Trichloroethylene and Tetrachloroethylene with Some Polar and Nonpolar Solvents
η	0.0009020	Pa×s	Ion Pair and Triple Ion Formation by Some Tetraalkylammonium Iodides in Binary Mixtures of Carbon Tetrachloride + Nitrobenzene
EA	[0.80; 2.12]	eV
EA	0.80 ± 0.34	eV	NIST
EA	2.00 ± 0.20	eV	NIST
EA	2.00 ± 0.20	eV	NIST
EA	2.12 ± 0.10	eV	NIST
εr	2.29		NCMS SOLV-DB
ΔfG°	[-58.28; -53.54]	kJ/mol
ΔfG°	-53.54	kJ/mol	ChemSep v8.3 pure component data
ΔfG°	-58.28	kJ/mol	KDB
Rg	3.4580		KDB
ΔfH°gas	[-125.00; -94.00]	kJ/mol
ΔfH°gas	-95.81	kJ/mol	ChemSep v8.3 pure component data
ΔfH°gas	-100.50	kJ/mol	KDB
ΔfH°gas	-95.60 ± 2.50	kJ/mol	NIST
ΔfH°gas	-94.00 ± 2.00	kJ/mol	NIST
ΔfH°gas	-115.00 ± 3.00	kJ/mol	NIST
ΔfH°gas	-125.00 ± 4.60	kJ/mol	NIST
ΔfH°gas	-103.00 ± 7.90	kJ/mol	NIST
ΔfH°liquid	[-128.40; -128.10]	kJ/mol
ΔfH°liquid	-128.10 ± 2.50	kJ/mol	NIST
ΔfH°liquid	-128.40	kJ/mol	NIST
ΔfusH°	7.72	kJ/mol	Joback Calculated Property
ΔvapH°	[29.96; 32.55]	kJ/mol
ΔvapH°	29.96	kJ/mol	NCMS SOLV-DB
ΔvapH°	32.54	kJ/mol	NIST
ΔvapH°	32.55 ± 0.07	kJ/mol	NIST
ΔvapH°	32.40	kJ/mol	NIST
ΔvapH°	32.54 ± 0.10	kJ/mol	NIST
ΔvapH°	32.43 ± 0.03	kJ/mol	NIST
ΔvapH°	32.41 ± 0.02	kJ/mol	NIST
ΔvapH°	30.00 ± 0.01	kJ/mol	NIST
IE	[11.00; 11.69]	eV
IE	11.47 ± 0.01	eV	NIST
IE	11.50 ± 0.10	eV	NIST
IE	11.30	eV	NIST
IE	11.47 ± 0.08	eV	NIST
IE	11.47	eV	NIST
IE	11.47 ± 0.01	eV	NIST
IE	Outlier 11.00 ± 1.00	eV	NIST
IE	11.69	eV	NIST
IE	11.69	eV	NIST
log10WS	[-2.31; -2.30]
log10WS	-2.30		Aq. Solubility Prediction
log10WS	-2.31		Estimated Solubility
logPoct/wat	2.830		NCMS SOLV-DB
McVol	73.910	ml/mol	McGowan Calculated Property
NFPA Health	4		KDB
Pc	[4493.00; 4557.60]	kPa
Pc	4557.00	kPa	ChemSep v8.3 pure component data
Pc	4516.00	kPa	KDB
Pc	4493.00 ± 50.00	kPa	NIST
Pc	4557.60 ± 10.13	kPa	NIST
Ptriple	1.12	kPa	ChemSep v8.3 pure component data
ρc	[556.84; 557.61]	kg/m3
ρc	556.84 ± 3.08	kg/m3	NIST
ρc	557.61 ± 3.08	kg/m3	NIST
ρc	557.61 ± 4.61	kg/m3	NIST
Inp	[611.00; 691.00]
Inp	680.50		NIST
Inp	660.00		NIST
Inp	680.70		NIST
Inp	680.00		NIST
Inp	667.00		NIST
Inp	673.00		NIST
Inp	662.00		NIST
Inp	648.00		NIST
Inp	680.00		NIST
Inp	672.00		NIST
Inp	Outlier 628.00		NIST
Inp	663.10		NIST
Inp	647.00		NIST
Inp	679.00		NIST
Inp	669.00		NIST
Inp	656.00		NIST
Inp	682.00		NIST
Inp	Outlier 691.00		NIST
Inp	671.00		NIST
Inp	657.00		NIST
Inp	645.70		NIST
Inp	661.00		NIST
Inp	663.00		NIST
Inp	652.00		NIST
Inp	661.00		NIST
Inp	Outlier 611.00		NIST
Inp	Outlier 618.00		NIST
Inp	651.00		NIST
Inp	675.00		NIST
Inp	659.00		NIST
Inp	656.00		NIST
Inp	663.00		NIST
Inp	661.00		NIST
Inp	654.00		NIST
Inp	645.00		NIST
Inp	645.00		NIST
Inp	658.00		NIST
Inp	661.00		NIST
Inp	664.00		NIST
Inp	658.00		NIST
Inp	645.00		NIST
Inp	645.00		NIST
Inp	661.00		NIST
Inp	659.00		NIST
Inp	664.00		NIST
Inp	646.00		NIST
Inp	658.00		NIST
Inp	672.00		NIST
Inp	673.00		NIST
Inp	659.00		NIST
Inp	649.00		NIST
Inp	659.00		NIST
Inp	645.00		NIST
Inp	658.00		NIST
Inp	645.70		NIST
Inp	680.50		NIST
Inp	673.00		NIST
Inp	Outlier 628.00		NIST
Inp	656.00		NIST
I	[864.00; 908.00]
I	900.66		NIST
I	902.20		NIST
I	886.54		NIST
I	888.00		NIST
I	895.00		NIST
I	868.00		NIST
I	879.00		NIST
I	908.00		NIST
I	900.00		NIST
I	900.00		NIST
I	864.00		NIST
I	886.00		NIST
I	888.00		NIST
I	886.00		NIST
I	872.00		NIST
S°liquid	[205.40; 219.20]	J/mol×K
S°liquid	214.39	J/mol×K	NIST
S°liquid	205.40	J/mol×K	NIST
S°liquid	219.20	J/mol×K	NIST
Tboil	[348.40; 419.40]	K
Tboil	349.79	K	ChemSep v8.3 pure component data
Tboil	349.90	K	KDB
Tboil	349.85	K	NCMS SOLV-DB
Tboil	350.20 ± 0.50	K	NIST
Tboil	349.84 ± 0.10	K	NIST
Tboil	349.00	K	NIST
Tboil	349.35 ± 0.30	K	NIST
Tboil	350.62 ± 0.05	K	NIST
Tboil	349.35 ± 0.50	K	NIST
Tboil	349.35 ± 0.50	K	NIST
Tboil	349.90	K	NIST
Tboil	349.98 ± 0.30	K	NIST
Tboil	349.98 ± 0.10	K	NIST
Tboil	350.10 ± 0.30	K	NIST
Tboil	349.90 ± 0.50	K	NIST
Tboil	349.85 ± 0.50	K	NIST
Tboil	349.60 ± 0.30	K	NIST
Tboil	349.84 ± 0.06	K	NIST
Tboil	350.00 ± 0.50	K	NIST
Tboil	348.70 ± 0.30	K	NIST
Tboil	349.85 ± 0.30	K	NIST
Tboil	349.85 ± 0.30	K	NIST
Tboil	349.88 ± 0.20	K	NIST
Tboil	349.60 ± 0.20	K	NIST
Tboil	349.85 ± 0.20	K	NIST
Tboil	349.80 ± 0.15	K	NIST
Tboil	349.85 ± 0.20	K	NIST
Tboil	349.85 ± 0.06	K	NIST
Tboil	349.90 ± 0.20	K	NIST
Tboil	349.55 ± 0.40	K	NIST
Tboil	349.80 ± 0.15	K	NIST
Tboil	349.90 ± 0.30	K	NIST
Tboil	349.85 ± 0.30	K	NIST
Tboil	349.90 ± 0.40	K	NIST
Tboil	350.10 ± 0.40	K	NIST
Tboil	349.90 ± 0.40	K	NIST
Tboil	349.85 ± 0.30	K	NIST
Tboil	349.76 ± 0.20	K	NIST
Tboil	349.83 ± 0.20	K	NIST
Tboil	350.05 ± 0.30	K	NIST
Tboil	349.85 ± 0.20	K	NIST
Tboil	349.00 ± 1.50	K	NIST
Tboil	349.45 ± 0.20	K	NIST
Tboil	349.80 ± 0.15	K	NIST
Tboil	349.95 ± 0.30	K	NIST
Tboil	349.85 ± 0.50	K	NIST
Tboil	350.15 ± 0.40	K	NIST
Tboil	350.05 ± 0.50	K	NIST
Tboil	349.90 ± 0.20	K	NIST
Tboil	349.81 ± 0.10	K	NIST
Tboil	349.65 ± 1.00	K	NIST
Tboil	349.90 ± 0.30	K	NIST
Tboil	349.90 ± 0.07	K	NIST
Tboil	349.90 ± 0.20	K	NIST
Tboil	349.75 ± 0.30	K	NIST
Tboil	349.90 ± 0.30	K	NIST
Tboil	349.15 ± 1.00	K	NIST
Tboil	349.94 ± 0.30	K	NIST
Tboil	349.90 ± 0.20	K	NIST
Tboil	349.85 ± 0.30	K	NIST
Tboil	349.75 ± 0.40	K	NIST
Tboil	Outlier 419.40 ± 0.40	K	NIST
Tboil	350.02 ± 0.30	K	NIST
Tboil	349.95 ± 0.30	K	NIST
Tboil	350.15 ± 0.50	K	NIST
Tboil	349.90 ± 0.30	K	NIST
Tboil	349.65 ± 0.50	K	NIST
Tboil	349.75 ± 0.50	K	NIST
Tboil	349.90 ± 0.30	K	NIST
Tboil	349.85 ± 0.20	K	NIST
Tboil	349.83 ± 0.05	K	NIST
Tboil	349.65 ± 0.30	K	NIST
Tboil	349.60 ± 0.50	K	NIST
Tboil	349.89 ± 0.05	K	NIST
Tboil	349.87 ± 0.15	K	NIST
Tboil	349.90 ± 0.25	K	NIST
Tboil	349.86 ± 0.30	K	NIST
Tboil	349.55 ± 0.20	K	NIST
Tboil	350.00 ± 0.20	K	NIST
Tboil	350.00 ± 0.20	K	NIST
Tboil	350.20 ± 0.60	K	NIST
Tboil	349.90 ± 0.40	K	NIST
Tboil	349.90 ± 0.50	K	NIST
Tboil	349.90 ± 0.50	K	NIST
Tboil	349.90 ± 0.50	K	NIST
Tboil	349.87 ± 0.20	K	NIST
Tboil	349.62 ± 0.30	K	NIST
Tboil	349.62 ± 0.20	K	NIST
Tboil	349.89 ± 0.30	K	NIST
Tboil	349.90 ± 0.20	K	NIST
Tboil	349.90 ± 0.20	K	NIST
Tboil	348.40 ± 1.50	K	NIST
Tc	[556.30; 558.35]	K
Tc	556.30	K	ChemSep v8.3 pure component data
Tc	556.60	K	KDB
Tc	556.36 ± 0.20	K	NIST
Tc	556.40	K	NIST
Tc	556.30 ± 0.20	K	NIST
Tc	Outlier 558.35 ± 5.00	K	NIST
Tfus	[240.39; 251.35]	K
Tfus	250.33	K	ChemSep v8.3 pure component data
Tfus	250.00	K	KDB
Tfus	250.16	K	Aq. Solubility Prediction
Tfus	250.15	K	NCMS SOLV-DB
Tfus	250.39 ± 0.01	K	NIST
Tfus	Outlier 240.39 ± 0.10	K	NIST
Tfus	250.38 ± 0.08	K	NIST
Tfus	250.42 ± 0.05	K	NIST
Tfus	250.55 ± 0.15	K	NIST
Tfus	Outlier 245.00 ± 1.00	K	NIST
Tfus	247.80 ± 1.00	K	NIST
Tfus	250.42 ± 0.04	K	NIST
Tfus	Outlier 245.40 ± 1.00	K	NIST
Tfus	250.30 ± 0.50	K	NIST
Tfus	250.41 ± 0.05	K	NIST
Tfus	250.30 ± 0.20	K	NIST
Tfus	250.36 ± 0.06	K	NIST
Tfus	250.40 ± 0.04	K	NIST
Tfus	250.25 ± 0.20	K	NIST
Tfus	250.16 ± 0.05	K	NIST
Tfus	250.45 ± 0.20	K	NIST
Tfus	251.35 ± 0.50	K	NIST
Tfus	250.50 ± 0.30	K	NIST
Tfus	250.00 ± 1.50	K	NIST
Tfus	250.00 ± 1.50	K	NIST
Tfus	250.28 ± 0.05	K	NIST
Tfus	250.31 ± 0.02	K	NIST
Tfus	250.28 ± 0.02	K	NIST
Tfus	250.30 ± 0.15	K	NIST
Tfus	250.20 ± 0.02	K	NIST
Tfus	250.18 ± 0.02	K	NIST
Tfus	250.18 ± 0.05	K	NIST
Tfus	250.18 ± 0.02	K	NIST
Tfus	250.17 ± 0.01	K	NIST
Tfus	250.26 ± 0.05	K	NIST
Tfus	249.92 ± 0.40	K	NIST
Tfus	250.01 ± 0.40	K	NIST
Tfus	250.10 ± 0.50	K	NIST
Tfus	250.20 ± 0.20	K	NIST
Tfus	248.45 ± 0.20	K	NIST
Tfus	250.19 ± 0.20	K	NIST
Ttriple	[226.10; 250.37]	K
Ttriple	Outlier 226.10	K	Solid binary mixtures of neopentanol with tert-Butyl chloride and carbon tetrachloride studied by thermal, X-ray and dielectric techniques
Ttriple	250.33	K	ChemSep v8.3 pure component data
Ttriple	250.25 ± 0.10	K	NIST
Ttriple	250.28 ± 0.02	K	NIST
Ttriple	245.70 ± 0.02	K	NIST
Ttriple	250.20 ± 0.20	K	NIST
Ttriple	250.30 ± 0.15	K	NIST
Ttriple	250.37 ± 0.20	K	NIST
Ttriple	249.00 ± 1.00	K	NIST
UQi	2.82		ChemSep v8.3 pure component data
URi	3.33		ChemSep v8.3 pure component data
Vc	[0.276; 0.276]	m3/kmol
Vc	0.276	m3/kmol	ChemSep v8.3 pure component data
Vc	0.276	m3/kmol	KDB
Zc	[0.2693290; 0.2710000]
Zc	0.2710000		ChemSep v8.3 pure component data
Zc	0.2693290		KDB
Zra	0.27		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[126.40; 133.90]	J/mol×K	[256.10; 340.00]
Cp,liquid	131.80	J/mol×K	256.10	NIST
Cp,liquid	130.40	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	130.60	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	130.70	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	130.90	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	126.40	J/mol×K	288.30	NIST
Cp,liquid	126.40	J/mol×K	288.30	NIST
Cp,liquid	133.90	J/mol×K	290.00	NIST
Cp,liquid	131.30	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	131.50	J/mol×K	293.00	NIST
Cp,liquid	129.80	J/mol×K	293.15	NIST
Cp,liquid	131.66	J/mol×K	293.15	NIST
Cp,liquid	128.00	J/mol×K	293.20	NIST
Cp,liquid	133.00	J/mol×K	298.00	NIST
Cp,liquid	128.80	J/mol×K	298.00	NIST
Cp,liquid	132.59	J/mol×K	298.00	NIST
Cp,liquid	133.10	J/mol×K	298.00	NIST
Cp,liquid	131.00	J/mol×K	298.00	NIST
Cp,liquid	132.20	J/mol×K	298.10	NIST
Cp,liquid	132.63	J/mol×K	298.10	NIST
Cp,liquid	130.50	J/mol×K	298.10	NIST
Cp,liquid	131.30	J/mol×K	298.15	NIST
Cp,liquid	131.67	J/mol×K	298.15	NIST
Cp,liquid	131.40	J/mol×K	298.15	NIST
Cp,liquid	131.90	J/mol×K	298.15	NIST
Cp,liquid	131.40	J/mol×K	298.15	NIST
Cp,liquid	130.80	J/mol×K	298.15	NIST
Cp,liquid	131.57	J/mol×K	298.15	NIST
Cp,liquid	131.36	J/mol×K	298.15	NIST
Cp,liquid	131.40	J/mol×K	298.15	NIST
Cp,liquid	131.60	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	133.35	J/mol×K	298.15	NIST
Cp,liquid	131.60	J/mol×K	298.15	NIST
Cp,liquid	131.34	J/mol×K	298.15	NIST
Cp,liquid	131.36	J/mol×K	298.15	NIST
Cp,liquid	132.90	J/mol×K	298.15	NIST
Cp,liquid	133.00	J/mol×K	298.15	NIST
Cp,liquid	131.60	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	130.90	J/mol×K	300.00	NIST
Cp,liquid	133.10	J/mol×K	301.20	NIST
Cp,liquid	128.90	J/mol×K	303.00	NIST
Cp,liquid	130.50	J/mol×K	303.30	NIST
Cp,liquid	132.00	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	132.50	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	132.90	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
Cp,liquid	133.40	J/mol×K	340.00	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,solid	44.22	J/mol×K	46.00	NIST
η	[0.0007600; 0.0261300]	Pa×s	[298.15; 313.15]
η	0.0261300	Pa×s	298.15	NCMS SOLV-DB
η	0.0008520	Pa×s	303.15	Studies of viscosities of dilute solutions of alkylamine in non-electrolyte solvents. II. Haloalkanes and other polar solvents
η	0.0008689	Pa×s	303.15	Viscosities and Densities of Binary Mixtures of 1,4-Dioxane, Carbon Tetrachloride, and Butanol at 303.15 K, 308.15 K, and 313.15 K
η	0.0008307	Pa×s	308.15	Viscosities and Densities of Binary Mixtures of 1,4-Dioxane, Carbon Tetrachloride, and Butanol at 303.15 K, 308.15 K, and 313.15 K
η	0.0007600	Pa×s	313.15	Studies of viscosities of dilute solutions of alkylamine in non-electrolyte solvents. II. Haloalkanes and other polar solvents
η	0.0008070	Pa×s	313.15	Viscosities and Densities of Binary Mixtures of 1,4-Dioxane, Carbon Tetrachloride, and Butanol at 303.15 K, 308.15 K, and 313.15 K
η	0.0008072	Pa×s	313.15	Viscosities and Densities of Binary Mixtures of 1,4-Dioxane, Carbon Tetrachloride, and Butanol at 303.15 K, 308.15 K, and 313.15 K
ΔfusH	[2.52; 4.63]	kJ/mol	[224.60; 250.50]
ΔfusH	4.60	kJ/mol	224.60	NIST
ΔfusH	4.58	kJ/mol	225.40	NIST
ΔfusH	4.63	kJ/mol	225.70	NIST
ΔfusH	2.69	kJ/mol	249.00	NIST
ΔfusH	2.69	kJ/mol	249.00	NIST
ΔfusH	2.52	kJ/mol	250.30	NIST
ΔfusH	2.56	kJ/mol	250.50	NIST
ΔsubH	[37.90; 43.30]	kJ/mol	[217.00; 237.50]
ΔsubH	38.80	kJ/mol	217.00	NIST
ΔsubH	43.30	kJ/mol	226.00	NIST
ΔsubH	37.90	kJ/mol	237.50	NIST
ΔvapH	[29.20; 33.70]	kJ/mol	[305.50; 524.50]
ΔvapH	33.70	kJ/mol	305.50	NIST
ΔvapH	32.30	kJ/mol	322.00	NIST
ΔvapH	31.70	kJ/mol	325.50	NIST
ΔvapH	30.00	kJ/mol	349.80	KDB
ΔvapH	29.82	kJ/mol	349.90	NIST
ΔvapH	30.40	kJ/mol	382.50	NIST
ΔvapH	29.20	kJ/mol	454.50	NIST
ΔvapH	30.60	kJ/mol	524.50	NIST
Pvap	[7.51; 93.32]	kPa	[283.15; 347.09]
Pvap	7.51	kPa	283.15	Total vapour pressure and excess Gibbs energy for binary mixtures of 1,1,2,2-tetrachloroethane or tetrachloroethene with tetrachloromethane at nine temperatures
Pvap	9.60	kPa	288.15	Total vapour pressure and excess Gibbs energy for binary mixtures of 1,1,2,2-tetrachloroethane or tetrachloroethene with tetrachloromethane at nine temperatures
Pvap	12.14	kPa	293.15	Total vapour pressure and excess Gibbs energy for binary mixtures of 1,1,2,2-tetrachloroethane or tetrachloroethene with tetrachloromethane at nine temperatures
Pvap	15.22	kPa	298.15	Total vapour pressure and excess Gibbs energy for binary mixtures of 1,1,2,2-tetrachloroethane or tetrachloroethene with tetrachloromethane at nine temperatures
Pvap	15.33	kPa	298.15	NCMS SOLV-DB
Pvap	18.83	kPa	303.15	Total Vapor Pressure Measurements for 2-Ethoxyethanol with Carbon Tetrachloride, Chloroform, and Dichloromethane at 303.15 K
Pvap	18.98	kPa	303.15	Total vapour pressure and excess Gibbs energy for binary mixtures of 1,1,2,2-tetrachloroethane or tetrachloroethene with tetrachloromethane at nine temperatures
Pvap	23.36	kPa	308.15	Total vapour pressure and excess Gibbs energy for binary mixtures of 1,1,2,2-tetrachloroethane or tetrachloroethene with tetrachloromethane at nine temperatures
Pvap	28.53	kPa	313.15	Total vapour pressure and excess Gibbs energy for binary mixtures of 1,1,2,2-tetrachloroethane or tetrachloroethene with tetrachloromethane at nine temperatures
Pvap	34.59	kPa	318.15	Total vapour pressure and excess Gibbs energy for binary mixtures of 1,1,2,2-tetrachloroethane or tetrachloroethene with tetrachloromethane at nine temperatures
Pvap	40.00	kPa	322.04	Determination and correlation of vapor liquid equilibrium for binary systems consisting of close-boiling components
Pvap	41.68	kPa	323.15	Total vapour pressure and excess Gibbs energy for binary mixtures of 1,1,2,2-tetrachloroethane or tetrachloroethene with tetrachloromethane at nine temperatures
Pvap	53.33	kPa	330.08	Determination and correlation of vapor liquid equilibrium for binary systems consisting of close-boiling components
Pvap	66.66	kPa	336.65	Determination and correlation of vapor liquid equilibrium for binary systems consisting of close-boiling components
Pvap	79.99	kPa	342.21	Determination and correlation of vapor liquid equilibrium for binary systems consisting of close-boiling components
Pvap	93.32	kPa	347.09	Determination and correlation of vapor liquid equilibrium for binary systems consisting of close-boiling components
n0	[1.45550; 1.45980]		[298.10; 303.15]
n0	1.45980		298.10	Excess Enthalpies and Thermal Conductivity Coefficients for Binary Mixtures of Carbon Tetrachloride and Four Alkanes (C5 to C8) at a Temperature of 298.15 K
n0	1.45740		298.15	Activity coefficients in binary mixtures formed by cyclohexanone with a variety of compounds at 94.7 kPa
n0	1.45715		298.15	Enthalpies of Vaporization and Sublimation of the Halogen-Substituted Aromatic Hydrocarbons at 298.15 K: Application of Solution Calorimetry Approach
n0	1.45700		298.15	NCMS SOLV-DB
n0	1.45550		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	[1575.00; 1584.30]	kg/m3	[298.00; 303.15]
ρl	1584.00	kg/m3	298.00	KDB
ρl	1583.80	kg/m3	298.15	Excess Molar volumes and Surface Tensions of Trimethylbenzene with Tetrahydrofuran Tetrachloromethane and Dimethylsulfoxide at 298.15 K
ρl	1584.30	kg/m3	298.15	Calorimetric Study of Nitrile Group-Solvent Interactions and Comparison with Dispersive Quasi-Chemical (DISQUAC) Predictions
ρl	1575.00	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
ΔfusS	[10.10; 20.50]	J/mol×K	[224.60; 250.50]
ΔfusS	20.49	J/mol×K	224.60	NIST
ΔfusS	20.30	J/mol×K	225.40	NIST
ΔfusS	20.50	J/mol×K	225.70	NIST
ΔfusS	10.82	J/mol×K	249.00	NIST
ΔfusS	10.10	J/mol×K	250.30	NIST
ΔfusS	10.20	J/mol×K	250.50	NIST
csound,fluid	[904.00; 932.00]	m/s	[293.00; 313.00]
csound,fluid	932.00	m/s	293.00	Ultrasonic velocity, viscosity and excess properties of binary mixture of tetrahydrofuran with 1-propanol and 2-propanol
csound,fluid	927.00	m/s	298.00	Ultrasonic velocity, viscosity and excess properties of binary mixture of tetrahydrofuran with 1-propanol and 2-propanol
csound,fluid	921.50	m/s	298.15	Compressibility studies of aqueous and CCl4 solutions of 18-crown-6 at T = 298.15 K
csound,fluid	921.70	m/s	298.15	Sound speed and density measurements for tetra-n-butylammonium bromide in benzene and carbon tetrachloride solutions at T = 298.15 K
csound,fluid	919.50	m/s	303.00	Ultrasonic velocity, viscosity and excess properties of binary mixture of tetrahydrofuran with 1-propanol and 2-propanol
csound,fluid	904.00	m/s	313.00	Ultrasonic velocity, viscosity and excess properties of binary mixture of tetrahydrofuran with 1-propanol and 2-propanol
γ	[0.02; 0.03]	N/m	[298.15; 313.15]
γ	0.02	N/m	298.15	Surface and bulk behavior of (dialkylsulfoxides + carbon tetrachloride) mixtures
γ	0.03	N/m	298.15	NCMS SOLV-DB
γ	0.03	N/m	298.20	KDB
γ	0.02	N/m	303.15	Surface and bulk behavior of (dialkylsulfoxides + carbon tetrachloride) mixtures
γ	0.02	N/m	308.15	Surface and bulk behavior of (dialkylsulfoxides + carbon tetrachloride) mixtures
γ	0.02	N/m	313.15	Surface and bulk behavior of (dialkylsulfoxides + carbon tetrachloride) mixtures

Datasets

1. Isobaric coefficient of expansion, 1/K (1)
2. Viscosity, Pa*s (1)
3. Speed of sound, m/s (1)

Isobaric coefficient of expansion, 1/K

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Isobaric coefficient of expansion, 1/K - Liquid
5000.00	278.15	0.0011
5000.00	288.15	0.0012
5000.00	298.15	0.0012
5000.00	308.15	0.0012
5000.00	318.15	0.0012
5000.00	328.15	0.0013
5000.00	338.15	0.0013
5000.00	348.15	0.0013
10000.00	278.15	0.0011
10000.00	288.15	0.0011
10000.00	298.15	0.0012
10000.00	308.15	0.0012
10000.00	318.15	0.0012
10000.00	328.15	0.0012
10000.00	338.15	0.0012
10000.00	348.15	0.0013
15000.00	278.15	0.0011
15000.00	288.15	0.0011
15000.00	298.15	0.0011
15000.00	308.15	0.0011
15000.00	318.15	0.0012
15000.00	328.15	0.0012
15000.00	338.15	0.0012
15000.00	348.15	0.0012
20000.00	278.15	0.0011
20000.00	288.15	0.0011
20000.00	298.15	0.0011
20000.00	308.15	0.0011
20000.00	318.15	0.0011
20000.00	328.15	0.0011
20000.00	338.15	0.0011
20000.00	348.15	0.0012
25000.00	278.15	0.0010
25000.00	288.15	0.0011
25000.00	298.15	0.0011
25000.00	308.15	0.0011
25000.00	318.15	0.0011
25000.00	328.15	0.0011
25000.00	338.15	0.0011
25000.00	348.15	0.0011
30000.00	278.15	0.0010
30000.00	288.15	0.0010
30000.00	298.15	0.0010
30000.00	308.15	0.0011
30000.00	318.15	0.0011
30000.00	328.15	0.0011
30000.00	338.15	0.0011
30000.00	348.15	0.0011
35000.00	278.15	0.0010
35000.00	288.15	0.0010
35000.00	298.15	0.0010
35000.00	308.15	0.0010
35000.00	318.15	0.0010
35000.00	328.15	0.0010
35000.00	338.15	0.0010
35000.00	348.15	0.0011
40000.00	278.15	0.0010
40000.00	288.15	0.0010
40000.00	298.15	0.0010
40000.00	308.15	0.0010
40000.00	318.15	0.0010
40000.00	328.15	0.0010
40000.00	338.15	0.0010
40000.00	348.15	0.0010
45000.00	278.15	0.0010
45000.00	288.15	0.0010
45000.00	298.15	0.0010
45000.00	308.15	0.0010
45000.00	318.15	0.0010
45000.00	328.15	0.0010
45000.00	338.15	0.0010
45000.00	348.15	0.0010
50000.00	278.15	0.0009
50000.00	288.15	0.0009
50000.00	298.15	0.0010
50000.00	308.15	0.0010
50000.00	318.15	0.0010
50000.00	328.15	0.0010
50000.00	338.15	0.0010
50000.00	348.15	0.0010
55000.00	278.15	0.0009
55000.00	288.15	0.0009
55000.00	298.15	0.0009
55000.00	308.15	0.0009
55000.00	318.15	0.0009
55000.00	328.15	0.0009
55000.00	338.15	0.0009
55000.00	348.15	0.0009
Reference

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
303.15	101.30	0.0008
Reference

Speed of sound, m/s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Speed of sound, m/s - Liquid
283.15	101.00	969.1
283.15	497.00	970.5
283.15	1065.00	972.7
283.15	2192.00	976.9
283.15	2306.00	977.4
283.15	3433.00	981.6
283.15	5102.00	987.7
283.15	5958.00	990.8
283.15	7972.00	998.0
283.15	8771.00	1000.6
283.15	9833.00	1004.6
283.15	11260.00	1009.5
283.15	12970.00	1015.5
283.15	13650.00	1017.6
283.15	16043.00	1026.0
283.15	19058.00	1035.9
283.15	22343.00	1046.6
283.15	25816.00	1057.5
283.15	30453.00	1071.7
298.15	101.00	921.1
298.15	583.00	923.1
298.15	865.00	924.2
298.15	887.00	924.4
298.15	1384.00	926.4
298.15	1731.00	927.8
298.15	1900.00	928.4
298.15	2056.00	929.1
298.15	2905.00	932.5
298.15	3020.00	933.0
298.15	3919.00	936.6
298.15	4367.00	938.4
298.15	4908.00	940.5
298.15	5436.00	942.6
298.15	5946.00	944.5
298.15	6868.00	948.0
298.15	7358.00	949.9
298.15	7761.00	951.5
298.15	8818.00	955.5
298.15	8930.00	955.9
298.15	9903.00	959.6
298.15	10321.00	961.2
298.15	11239.00	964.6
298.15	12541.00	969.3
298.15	13397.00	972.5
298.15	14945.00	978.0
298.15	15313.00	979.4
298.15	17404.00	986.8
298.15	17674.00	987.8
298.15	20253.00	996.7
298.15	20404.00	997.2
298.15	22533.00	1004.5
298.15	24855.00	1012.3
298.15	24984.00	1012.8
298.15	25186.00	1013.4
298.15	27693.00	1021.7
298.15	29953.00	1029.0
298.15	30569.00	1030.8
298.15	101.00	921.1
313.15	101.00	874.2
313.15	108.00	874.2
313.15	478.00	875.9
313.15	894.00	877.7
313.15	1827.00	881.9
313.15	2938.00	886.7
313.15	4119.00	891.6
313.15	5135.00	896.1
313.15	5591.00	898.0
313.15	6975.00	903.6
313.15	8334.00	909.4
313.15	10049.00	916.2
313.15	12992.00	927.9
313.15	14421.00	933.4
313.15	16421.00	941.1
313.15	18812.00	949.9
313.15	20514.00	956.3
313.15	25209.00	972.9
313.15	31645.00	994.8
333.15	101.00	813.0
333.15	967.00	817.4
333.15	1691.00	820.9
333.15	2195.00	823.4
333.15	3177.00	828.1
333.15	5118.00	837.4
333.15	5595.00	839.5
333.15	7312.00	847.3
333.15	8236.00	851.5
333.15	9201.00	855.8
333.15	10593.00	862.0
333.15	11851.00	867.4
333.15	13131.00	872.9
333.15	14740.00	879.6
333.15	15989.00	884.8
333.15	17758.00	892.1
333.15	19476.00	898.9
333.15	20905.00	904.6
333.15	22422.00	910.5
333.15	25433.00	922.0
333.15	27880.00	931.1
333.15	31372.00	943.7
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[38.48; 107.12]	J/mol×K	[50.00; 1500.00]	ChemSep v8.3 pure component data
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K
Coefficient A			3.75880e+01
Coefficient B			-2.42531e+02
Coefficient C			4.75950e+00
Coefficient D			-4.46049e-04
Coefficient E			1.39110e-07
Comment			ChemSep eq 16, IdealGasHeatCapacityCp
Temperature range, min.			50.00
Temperature range, max.			1500.00
Cp,gas	38.48	J/mol×K	50.00	Calculated Property
Cp,gas	71.46	J/mol×K	211.11	Calculated Property
Cp,gas	90.11	J/mol×K	372.22	Calculated Property
Cp,gas	98.32	J/mol×K	533.33	Calculated Property
Cp,gas	102.15	J/mol×K	694.44	Calculated Property
Cp,gas	104.02	J/mol×K	855.56	Calculated Property
Cp,gas	105.03	J/mol×K	1016.67	Calculated Property
Cp,gas	105.70	J/mol×K	1177.78	Calculated Property
Cp,gas	106.34	J/mol×K	1338.89	Calculated Property
Cp,gas	107.12	J/mol×K	1500.00	Calculated Property
Cp,gas	[82.65; 108.31]	J/mol×K	[298.00; 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			1.03113e+02
Coefficient B			4.18864e+00
Coefficient C			-1.12647e+00
Coefficient D			9.56770e-02
Coefficient E			-1.91962e+00
Reference			Chase, 1998
Comment			F=-133.3357, G=422.4334, H=-95.98096; Data last reviewed in December, 1968
Temperature range, min.			298.00
Temperature range, max.			6000.00
Cp,gas	82.65	J/mol×K	298.00	Calculated Property
Cp,gas	103.90	J/mol×K	931.56	Calculated Property
Cp,gas	106.49	J/mol×K	1565.11	Calculated Property
Cp,gas	107.50	J/mol×K	2198.67	Calculated Property
Cp,gas	107.87	J/mol×K	2832.22	Calculated Property
Cp,gas	107.92	J/mol×K	3465.78	Calculated Property
Cp,gas	107.83	J/mol×K	4099.33	Calculated Property
Cp,gas	107.76	J/mol×K	4732.89	Calculated Property
Cp,gas	107.87	J/mol×K	5366.44	Calculated Property
Cp,gas	108.31	J/mol×K	6000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[129.91; 164.02]	J/mol×K	[250.33; 388.71]	ChemSep v8.3 pure component data
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K
Coefficient A			1.29390e+02
Coefficient B			1.95920e+03
Coefficient C			-2.57408e+01
Coefficient D			8.08340e-02
Coefficient E			-4.74910e-05
Comment			ChemSep eq 16, LiquidHeatCapacityCp
Temperature range, min.			250.33
Temperature range, max.			388.71
Cp,liquid	129.91	J/mol×K	250.33	Calculated Property
Cp,liquid	130.18	J/mol×K	265.71	Calculated Property
Cp,liquid	130.61	J/mol×K	281.08	Calculated Property
Cp,liquid	131.32	J/mol×K	296.46	Calculated Property
Cp,liquid	132.49	J/mol×K	311.83	Calculated Property
Cp,liquid	134.40	J/mol×K	327.21	Calculated Property
Cp,liquid	137.53	J/mol×K	342.58	Calculated Property
Cp,liquid	142.62	J/mol×K	357.96	Calculated Property
Cp,liquid	150.85	J/mol×K	373.33	Calculated Property
Cp,liquid	164.02	J/mol×K	388.71	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0020666; 0.0001811]	Pa×s	[250.00; 473.00]	ChemSep v8.3 pure component data
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-2.22970e+01
Coefficient B			1.64500e+03
Coefficient C			1.75880e+00
Coefficient D			-2.81630e-06
Coefficient E			2.00000e+00
Comment			ChemSep eq 101, LiquidViscosity
Temperature range, min.			250.00
Temperature range, max.			473.00
η	0.0020666	Pa×s	250.00	Calculated Property
η	0.0012997	Pa×s	274.78	Calculated Property
η	0.0008858	Pa×s	299.56	Calculated Property
η	0.0006411	Pa×s	324.33	Calculated Property
η	0.0004857	Pa×s	349.11	Calculated Property
η	0.0003813	Pa×s	373.89	Calculated Property
η	0.0003077	Pa×s	398.67	Calculated Property
η	0.0002537	Pa×s	423.44	Calculated Property
η	0.0002129	Pa×s	448.22	Calculated Property
η	0.0001811	Pa×s	473.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[34.64; 6.52]	kJ/mol	[250.33; 553.15]	ChemSep v8.3 pure component data
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			3.17640e+01
Coefficient B			-1.57290e+00
Coefficient C			5.21580e+00
Coefficient D			-5.52590e+00
Coefficient E			2.19310e+00
Critical temperature, Tc (K)			5.56300e+02
Comment			ChemSep eq 106, HeatOfVaporization
Temperature range, min.			250.33
Temperature range, max.			553.15
ΔvapH	34.64	kJ/mol	250.33	Calculated Property
ΔvapH	33.12	kJ/mol	283.98	Calculated Property
ΔvapH	31.45	kJ/mol	317.62	Calculated Property
ΔvapH	29.64	kJ/mol	351.27	Calculated Property
ΔvapH	27.68	kJ/mol	384.92	Calculated Property
ΔvapH	25.50	kJ/mol	418.56	Calculated Property
ΔvapH	22.96	kJ/mol	452.21	Calculated Property
ΔvapH	19.81	kJ/mol	485.86	Calculated Property
ΔvapH	15.47	kJ/mol	519.50	Calculated Property
ΔvapH	6.52	kJ/mol	553.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.12; 4557.34]	kPa	[250.33; 556.35]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.41285e+01
Coefficient B			-2.94375e+03
Coefficient C			-4.02620e+01
Temperature range, min.			250.33
Temperature range, max.			556.35
Pvap	1.12	kPa	250.33	Calculated Property
Pvap	7.90	kPa	284.33	Calculated Property
Pvap	34.54	kPa	318.33	Calculated Property
Pvap	109.47	kPa	352.34	Calculated Property
Pvap	276.55	kPa	386.34	Calculated Property
Pvap	591.92	kPa	420.34	Calculated Property
Pvap	1118.06	kPa	454.34	Calculated Property
Pvap	1917.58	kPa	488.35	Calculated Property
Pvap	3047.83	kPa	522.35	Calculated Property
Pvap	4557.34	kPa	556.35	Calculated Property
Pvap	[0.05; 4538.15]	kPa	[213.45; 556.35]	ChemSep v8.3 pure component data
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K
Coefficient A			7.57632e+01
Coefficient B			-6.30420e+03
Coefficient C			-9.22470e+00
Coefficient D			7.43520e-06
Coefficient E			2.00000e+00
Comment			ChemSep eq 101, VaporPressure
Temperature range, min.			213.45
Temperature range, max.			556.35
Pvap	0.05	kPa	213.45	Calculated Property
Pvap	1.20	kPa	251.55	Calculated Property
Pvap	10.28	kPa	289.65	Calculated Property
Pvap	49.17	kPa	327.75	Calculated Property
Pvap	160.86	kPa	365.85	Calculated Property
Pvap	407.48	kPa	403.95	Calculated Property
Pvap	865.50	kPa	442.05	Calculated Property
Pvap	1625.44	kPa	480.15	Calculated Property
Pvap	2799.56	kPa	518.25	Calculated Property
Pvap	4538.15	kPa	556.35	Calculated Property
Pvap	[1.09; 4527.13]	kPa	[250.00; 556.35]	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			7.49948e+01
Coefficient B			-6.26338e+03
Coefficient C			-9.11397e+00
Coefficient D			7.41145e-06
Coefficient E			0.00000e+00
Temperature range, min.			250.00
Temperature range, max.			556.35
Pvap	1.09	kPa	250.00	Calculated Property
Pvap	7.81	kPa	284.04	Calculated Property
Pvap	34.33	kPa	318.08	Calculated Property
Pvap	107.98	kPa	352.12	Calculated Property
Pvap	269.12	kPa	386.16	Calculated Property
Pvap	568.26	kPa	420.19	Calculated Property
Pvap	1064.51	kPa	454.23	Calculated Property
Pvap	1827.52	kPa	488.27	Calculated Property
Pvap	2943.77	kPa	522.31	Calculated Property
Pvap	4527.13	kPa	556.35	Calculated Property
Pvap	[12.09; 104.39]	kPa	[293.03; 350.86]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.38683e+01
Coefficient B			-2.81325e+03
Coefficient C			-4.57390e+01
Reference			Hildenbrand and McDonald, 1959, 2
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			293.03
Temperature range, max.			350.86
Pvap	12.09	kPa	293.03	Calculated Property
Pvap	16.12	kPa	299.46	Calculated Property
Pvap	21.20	kPa	305.88	Calculated Property
Pvap	27.51	kPa	312.31	Calculated Property
Pvap	35.27	kPa	318.73	Calculated Property
Pvap	44.70	kPa	325.16	Calculated Property
Pvap	56.06	kPa	331.58	Calculated Property
Pvap	69.60	kPa	338.01	Calculated Property
Pvap	85.61	kPa	344.43	Calculated Property
Pvap	104.39	kPa	350.86	Calculated Property
Pvap	[12.09; 104.39]	kPa	[293.03; 350.86]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.38683e+01
Coefficient B			-2.81325e+03
Coefficient C			-4.57390e+01
Reference			Hildenbrand and McDonald, 1959
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			293.03
Temperature range, max.			350.86
Pvap	12.09	kPa	293.03	Calculated Property
Pvap	16.12	kPa	299.46	Calculated Property
Pvap	21.20	kPa	305.88	Calculated Property
Pvap	27.51	kPa	312.31	Calculated Property
Pvap	35.27	kPa	318.73	Calculated Property
Pvap	44.70	kPa	325.16	Calculated Property
Pvap	56.06	kPa	331.58	Calculated Property
Pvap	69.60	kPa	338.01	Calculated Property
Pvap	85.61	kPa	344.43	Calculated Property
Pvap	104.39	kPa	350.86	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[1669.69; 723.12]	kg/m3	[250.33; 554.70]	ChemSep v8.3 pure component data
Equation			Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K
Coefficient A			1.64913e+02
Coefficient B			2.83280e-01
Coefficient C			5.56300e+02
Coefficient D			3.00920e-01
Comment			ChemSep eq 105, LiquidDensity
Temperature range, min.			250.33
Temperature range, max.			554.70
ρl	1669.69	kg/m3	250.33	Calculated Property
ρl	1609.86	kg/m3	284.15	Calculated Property
ρl	1547.02	kg/m3	317.97	Calculated Property
ρl	1480.45	kg/m3	351.79	Calculated Property
ρl	1409.07	kg/m3	385.61	Calculated Property
ρl	1331.23	kg/m3	419.42	Calculated Property
ρl	1244.09	kg/m3	453.24	Calculated Property
ρl	1141.95	kg/m3	487.06	Calculated Property
ρl	1009.72	kg/m3	520.88	Calculated Property
ρl	723.12	kg/m3	554.70	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 8.74e-04]	N/m	[250.33; 540.24]	ChemSep v8.3 pure component data
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K
Coefficient A			-1.00750e-02
Coefficient B			1.36760e+02
Coefficient C			-4.06870e+00
Coefficient D			3.80540e-03
Coefficient E			-9.43870e-06
Comment			ChemSep eq 16, SurfaceTension
Temperature range, min.			250.33
Temperature range, max.			540.24
γ	0.03	N/m	250.33	Calculated Property
γ	0.03	N/m	282.54	Calculated Property
γ	0.02	N/m	314.75	Calculated Property
γ	0.02	N/m	346.97	Calculated Property
γ	0.02	N/m	379.18	Calculated Property
γ	0.01	N/m	411.39	Calculated Property
γ	0.01	N/m	443.60	Calculated Property
γ	0.01	N/m	475.82	Calculated Property
γ	0.00	N/m	508.03	Calculated Property
γ	8.74e-04	N/m	540.24	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λ	[0.00; 0.05]	W/m×K	[250.33; 1000.00]	ChemSep v8.3 pure component data
Equation			Y = A·T^B / (1 + C/T + D/T²) Y is λ in W/m×K, T in K
Coefficient A			1.20800e-04
Coefficient B			9.85410e-01
Coefficient C			1.41110e+03
Coefficient D			-3.65840e+04
Comment			ChemSep eq 102, VaporThermalConductivity
Temperature range, min.			250.33
Temperature range, max.			1000.00
λ	0.00	W/m×K	250.33	Calculated Property
λ	0.01	W/m×K	333.63	Calculated Property
λ	0.01	W/m×K	416.92	Calculated Property
λ	0.02	W/m×K	500.22	Calculated Property
λ	0.02	W/m×K	583.52	Calculated Property
λ	0.02	W/m×K	666.81	Calculated Property
λ	0.03	W/m×K	750.11	Calculated Property
λ	0.03	W/m×K	833.41	Calculated Property
λ	0.04	W/m×K	916.70	Calculated Property
λ	0.05	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λ	[0.11; 0.08]	W/m×K	[250.33; 428.15]	ChemSep v8.3 pure component data
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is λ in W/m×K, T in K
Coefficient A			3.44320e-02
Coefficient B			-2.27950e+02
Coefficient C			-3.81170e-01
Coefficient D			-4.83710e-03
Coefficient E			-1.17820e-06
Comment			ChemSep eq 16, LiquidThermalConductivity
Temperature range, min.			250.33
Temperature range, max.			428.15
λ	0.11	W/m×K	250.33	Calculated Property
λ	0.11	W/m×K	270.09	Calculated Property
λ	0.10	W/m×K	289.85	Calculated Property
λ	0.10	W/m×K	309.60	Calculated Property
λ	0.10	W/m×K	329.36	Calculated Property
λ	0.09	W/m×K	349.12	Calculated Property
λ	0.09	W/m×K	368.88	Calculated Property
λ	0.08	W/m×K	388.63	Calculated Property
λ	0.08	W/m×K	408.39	Calculated Property
λ	0.08	W/m×K	428.15	Calculated Property

Similar Compounds

Find more compounds similar to Carbon Tetrachloride.

Mixtures

• 1-Propanol, 2,2-dimethyl- + Carbon Tetrachloride
• Benzenamine, 4-methyl-2-nitro- + Carbon Tetrachloride
• Propylamine + Carbon Tetrachloride
• 1-Butanamine + Carbon Tetrachloride
• 1-Butanamine, N-butyl- + Carbon Tetrachloride
• 1-Propanamine, N,N-dipropyl- + Carbon Tetrachloride
• Cyclohexanone + Carbon Tetrachloride
• Dimethyl Sulfoxide + Carbon Tetrachloride
• Carbon Tetrachloride + diethyl sulfoxide
• Propane, 1,1'-sulfinylbis- + Carbon Tetrachloride
• Butane, 1,1'-sulfinylbis- + Carbon Tetrachloride
• Tetra-N-butylammonium bromide + Carbon Tetrachloride
• Carbon Tetrachloride + Tetrahydrofuran
• Carbon Tetrachloride + Ethane, 1,1,2,2-tetrachloro-
• Tetrachloroethylene + Carbon Tetrachloride
• 2-Methyl-6-nitroaniline + Carbon Tetrachloride
• Acetic acid, chloro-, ethyl ester + Carbon Tetrachloride
• Diethyl malonate + Carbon Tetrachloride
• Propanedioic acid, bromo-, diethyl ester + Carbon Tetrachloride
• D-Fenchone + Carbon Tetrachloride

Find more mixtures with Carbon Tetrachloride.

Sources

• KDB Vapor Pressure Data
• 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.
• Total vapour pressure and excess Gibbs energy for binary mixtures of 1,1,2,2-tetrachloroethane or tetrachloroethene with tetrachloromethane at nine temperatures
• Activity coefficients in binary mixtures formed by cyclohexanone with a variety of compounds at 94.7 kPa
• Ultrasonic velocity, viscosity and excess properties of binary mixture of tetrahydrofuran with 1-propanol and 2-propanol
• Determination and correlation of vapor liquid equilibrium for binary systems consisting of close-boiling components
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
• Activity coefficients at infinite dilution of organic solutes in 1-octyl-3-methylimidazolium nitrate using gas-liquid chromatography
• Using binary mixtures of dicationic ionic liquids for determination ofactivity coefficients at infinite dilution by gas-liquid chromatography
• Experimental and theoretical study of interaction between organic compounds and 1- (4-sulfobutyl)-3-methylimidazolium based ionic liquids
• Study of interaction between organic compounds and mono or dicationic oxygenated ionic liquids using gas chromatography
• Speed of sound in liquid tetrachloromethane and benzene at temperatures from 283.15 K to 333.15 K and pressures up to 30 MPa
• 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
• 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
• Compressibility studies of aqueous and CCl4 solutions of 18-crown-6 at T = 298.15 K
• Sound speed and density measurements for tetra-n-butylammonium bromide in benzene and carbon tetrachloride solutions at T = 298.15 K
• Determination of solvation and specific interaction enthalpies of adamantane derivatives in aprotic solvents
• Measurement of activity coefficients at infinite dilution in 1-hexadecyl-3-methylimidazolium tetrafluoroborate ionic liquid
• Surface and bulk behavior of (dialkylsulfoxides + carbon tetrachloride) mixtures
• Thermodynamic properties of chiral fenchones in some solutions at T = 298.15 K
• Interactions of volatile organic compounds with the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
• Interactions of volatile organic compounds with the ionic liquids 1-butyl-1-methylpyrrolidinium tetracyanoborate and 1-butyl-1-methylpyrrolidinium bis(oxalato)borate
• Infinite dilution activity coefficients of volatile organic compounds in two ionic liquids composed of the tris(pentafluoroethyl) trifluorophosphate ([FAP]) anion and a functionalized cation
• Activity coefficients at infinite dilution of organic solutes in 1-hexyl-3- methylimidazolium trifluoroacetate and influence of interfacial adsorption using gas liquid chromatography
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-butyl-3-methylimidazolium methyl sulfate
• Solvation parameter model and thermodynamic parameters in a dicationic ionic liquid based on pyrrolidinium
• Activity coefficients at infinite dilution of organic solutes in methylphosphonate based ionic liquids using gas-liquid chromatography
• Solubility determination and thermodynamic modeling of 5-nitro-8- hydroxyquinoline in ten organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
• Solubility and solution thermodynamics of 2-methyl-6-nitroaniline in ten organic solvents at elevated temperatures
• Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-hexyl-2,3-dimethylimidazolium bis(trifluoromethylsulfonyl)imide
• Solubility of 4-methyl-2-nitroaniline in fourteen organic solvents from T = (278.15 to 313.15) 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 binary mixtures based on gamma infinity data using [OMMIM][NTf2] ionic liquid and modelling of thermodynamic functions
• 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
• 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
• Thermochemical behaviour of straight-chain ethers CH3O(CH2CH2O)nCH3 (n = 1 4) in aqueous and tetrachlormethane solutions
• Solution Enthalpies of 1,4-Dioxane: Study of Solvent Effects Through Quantitative Structure-Property Relationships
• Use of quantitative structure property relationships to study the solvation process of 18-crown-6
• 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
• New method for determination of vaporization and sublimation enthalpy of aromatic compounds at 298.15 K using solution calorimetry technique and group-additivity scheme
• Solid binary mixtures of neopentanol with tert-Butyl chloride and carbon tetrachloride studied by thermal, X-ray and dielectric techniques
• Solution and solvation enthalpies of aromatic derivitives in binary mixtures. Dipole moment and dielectric properties
• Solubility of Halogenated Hydrocarbons in Hydrophobic Ionic Liquids: Experimental Study and COSMO-RS Prediction
• Relative Permittivity and Apparent Dipole Moments of Nitromethane, Nitroethane, 1-Nitropropane and 2- Nitropropane in Several Nonpolar Solvents.
• 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
• 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
• Determination of Infinite Dilution Activity Coefficients of Several Organic Solutes in N-Butylpyridinium Nitrate/N-Octylpyridinium Nitrate by Blend Inverse Gas Chromatography
• Measurement and Correlation of Solubility of Two Isomers of Cyanopyridine in Eight Pure Solvents from 268.15 K 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
• Measurement and Correlation of the Dissolution Equilibria of o-Iodoaniline and p-Iodoaniline in Pure Solvents
• Solubility Determination and Thermodynamic Modeling of Glutaric Anhydride in Diverse Solvent Systems Consisting of Acetic Acid, Ethanoic Anhydride, and Tetrachloromethane from T = (278.45 to 324.45) K
• Solubilities of Organic Semiconductors and Nonsteroidal Anti-inflammatory Drugs in Pure and Mixed Organic Solvents: Measurement and Modeling with Hansen Solubility Parameter
• Thermodynamic Parameters of a New Synthesized Tricationic Ionic Liquid Stationary Phase by Inverse Gas Chromatography
• Determination of Activity Coefficients at Infinite Dilution of Solutes in N,N'-Di(2-ethylhexyl)isobutyramide Using Inverse Gas-Liquid Chromatography
• Thermodynamic Studies of Solubility for Naphthalene in 12 Solvents from 279 to 330 K
• 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
• Viscosities and Densities of Binary Mixtures of 1,4-Dioxane, Carbon Tetrachloride, and Butanol at 303.15 K, 308.15 K, and 313.15 K
• Solubility in Binary Solvent Mixtures: Anthracene Dissolved in Alcohol + Carbon Tetrachloride Mixtures at 298.2 K
• Solubility of Benzophenone in Binary Alkane + Carbon Tetrachloride Solvent Mixtures
• Total Vapor Pressure Measurements for 2-Ethoxyethanol with Carbon Tetrachloride, Chloroform, and Dichloromethane at 303.15 K
• Viscosity Behavior of 18-Crown-6 in Aqueous and Carbon Tetrachloride Solutions at Different Temperatures and at Ambient Pressure
• Densities and Viscosities of Binary Liquid Mixtures of Trichloroethylene and Tetrachloroethylene with Some Polar and Nonpolar Solvents
• Phase Separation in Binary Mixtures Containing Linear Perfluoroalkanes
• Excess Molar volumes and Surface Tensions of Trimethylbenzene with Tetrahydrofuran Tetrachloromethane and Dimethylsulfoxide at 298.15 K
• Measurement of Diffusion Coefficients in Thermodynamically Nonideal Systems
• 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
• 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 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
• Calorimetric Study of Nitrile Group-Solvent Interactions and Comparison with Dispersive Quasi-Chemical (DISQUAC) Predictions
• Activity Coefficients at Infinite Dilution for Hydrocarbons in Fatty Alcohols Determined by Gas-Liquid Chromatography
• Activity Coefficients at Infinite Dilution in Methylimidazolium Nitrate Ionic Liquids
• High Pressure Phase Behavior of Carbon Dioxide in Carbon Disulfide and Carbon Tetrachloride
• 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
• 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
• 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
• Solid Liquid Phase Equilibrium and Solubility of Dibenzo[b,d]furan and 9H-Fluoren-9-one in Organic Solvents
• 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
• 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 and Thermodynamic Study of Carbon Tetrachloride in Imidazolium Ionic Liquids at Different Temperatures
• Solubility of Dichloronitrobenzene in Eight Organic Solvents from T = (278.15 to 303.15) K: Measurement and Thermodynamic Modeling
• 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
• Measurement, Correlation, and Thermodynamics Parameters of Biological Active Pyrimidine Derivatives in Organic Solvents at Different Temperatures
• Enthalpies of Vaporization and Sublimation of the Halogen-Substituted Aromatic Hydrocarbons at 298.15 K: Application of Solution Calorimetry Approach
• Solubility of Salicylic Acid in Water, Ethanol, Carbon Tetrachloride, Ethyl Acetate, and Xylene
• 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
• Excess Enthalpies and Thermal Conductivity Coefficients for Binary Mixtures of Carbon Tetrachloride and Four Alkanes (C5 to C8) at a Temperature of 298.15 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
• Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Inverse Gas Chromatography
• Activity Coefficients at Infinite Dilution of Organic Compounds in Trihexyl(tetradecyl)phosphonium Bis(trifluoromethylsulfonyl)imide Using Inverse Gas Chromatography
• Ion Pair and Triple Ion Formation by Some Tetraalkylammonium Iodides in Binary Mixtures of Carbon Tetrachloride + Nitrobenzene
• Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
• Solubilities of 3-Pentadecylphenol in Ethanol, 1-Butanol, Toluene, Acetone, Tetrachloromethane, and Ethyl Acetate
• Solubility of Ofloxacin in 1,2-Dichloromethane, Chloroform, Carbon Tetrachloride, and Water from (293.15 to 313.15) K
• Solubility of 5-Amino Salicylic Acid in Different Solvents at Various Temperatures
• Isobaric Thermal Expansivity for Nonpolar Compounds
• Study of Ether-, Alcohol-, or Cyano-Functionalized Ionic Liquids Using Inverse Gas Chromatography
• 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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