Chemical Properties of Methylene chloride (CAS 75-09-2)

InChI

InChI=1S/CH2Cl2/c2-1-3/h1H2

InChI Key

YMWUJEATGCHHMB-UHFFFAOYSA-N

Formula

CH2Cl2

SMILES

ClCCl

Molecular Weight¹

84.93

CAS

75-09-2

Other Names

• Aerothene MM
• CH2Cl2
• Chlorure de methylene
• F 30
• F 30 (chlorocarbon)
• Freon 30
• HCC 30
• Khladon 30
• Metaclen
• Methane dichloride
• Methane, dichloro-
• Methoklone
• Methylene bichloride
• Metylenu chlorek
• NCI-C50102
• NSC 406122
• Narkotil
• R 30
• R-30
• Rcra waste number U080
• Salesthin
• Solaesthin
• Soleana VDA
• Solmethine
• UN 1593
• dichloromethane
• methylene dichloride

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• T_ig : Autoignition Temperature (K).
• BasG : Gas basicity (kJ/mol).
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• 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).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• NFPA Safety : NFPA Safety Rating.
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I_p : Polar retention indices.
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• 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).
• T_fus : Normal melting (fusion) point (K).
• V_c : Critical Volume (m³/kmol).
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	[0.1990; 0.2027]
ω	0.2027		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.1990		KDB
PAff	628.00 ± 8.00	kJ/mol	NIST
Tig	829.15	K	NCMS SOLV-DB
BasG	602.00 ± 8.00	kJ/mol	NIST
ΔcH°liquid	[-605.80; -602.50]	kJ/mol
ΔcH°liquid	-602.50	kJ/mol	NIST
ΔcH°liquid	-605.80 ± 8.40	kJ/mol	NIST
μ	1.80	debye	KDB
εr	8.93		NCMS SOLV-DB
ΔfG°	-68.91	kJ/mol	KDB
Rg	2.4320		KDB
ΔfH°gas	[-95.70; -94.68]	kJ/mol
ΔfH°gas	-94.68 ± 0.60	kJ/mol	Active Thermochemical Tables 1.112, gas-phase enthalpies of formation Compiled value
ΔfH°gas	-95.46	kJ/mol	KDB
ΔfH°gas	-95.10 ± 2.50	kJ/mol	NIST
ΔfH°gas	-95.70 ± 1.30	kJ/mol	NIST
ΔfH°liquid	[-124.30; -124.10]	kJ/mol
ΔfH°liquid	-124.10 ± 2.50	kJ/mol	NIST
ΔfH°liquid	-124.30	kJ/mol	NIST
ΔfusH°	6.74	kJ/mol	Joback Calculated Property
ΔvapH°	[28.50; 30.60]	kJ/mol
ΔvapH°	28.53	kJ/mol	NCMS SOLV-DB
ΔvapH°	29.00	kJ/mol	NIST
ΔvapH°	29.03 ± 0.08	kJ/mol	NIST
ΔvapH°	Outlier 30.60 ± 0.10	kJ/mol	NIST
ΔvapH°	28.80	kJ/mol	NIST
ΔvapH°	28.50 ± 0.42	kJ/mol	NIST
IE	[11.28; 11.40]	eV
IE	11.33 ± 0.04	eV	NIST
IE	11.32	eV	NIST
IE	11.40	eV	NIST
IE	11.32 ± 0.01	eV	NIST
IE	11.28	eV	NIST
IE	11.33	eV	NIST
IE	11.36	eV	NIST
IE	11.35 ± 0.02	eV	NIST
IE	11.40	eV	NIST
log10WS	[-0.63; -0.63]
log10WS	-0.63		Aq. Solubility Prediction
log10WS	-0.63		Estimated Solubility
logPoct/wat	1.250		NCMS SOLV-DB
McVol	49.430	ml/mol	McGowan Calculated Property
NFPA Fire	1		NCMS SOLV-DB
NFPA Health	[%!d(float64=2); %!d(float64=2)]
NFPA Health	2		KDB
NFPA Health	2		NCMS SOLV-DB
NFPA Safety	0		NCMS SOLV-DB
Pc	[6100.00; 6355.00]	kPa
Pc	6350.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 10 Compiled value
Pc	6355.00	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	6100.00	kPa	KDB
Pc	6355.00 ± 15.00	kPa	NIST
Inp	[477.00; 555.90]
Inp	Outlier 553.50		NIST
Inp	Outlier 555.90		NIST
Inp	Outlier 553.70		NIST
Inp	548.40		NIST
Inp	542.20		NIST
Inp	506.30		NIST
Inp	518.00		NIST
Inp	504.90		NIST
Inp	508.00		NIST
Inp	516.90		NIST
Inp	516.50		NIST
Inp	537.80		NIST
Inp	537.90		NIST
Inp	519.00		NIST
Inp	520.00		NIST
Inp	518.00		NIST
Inp	Outlier 486.00		NIST
Inp	524.00		NIST
Inp	497.90		NIST
Inp	Outlier 477.00		NIST
Inp	511.00		NIST
Inp	513.00		NIST
Inp	531.00		NIST
Inp	540.00		NIST
Inp	540.00		NIST
Inp	510.00		NIST
Inp	512.70		NIST
Inp	531.60		NIST
Inp	524.00		NIST
Inp	520.00		NIST
Inp	Outlier 480.00		NIST
Inp	Outlier 488.00		NIST
Inp	531.00		NIST
Inp	531.00		NIST
Inp	528.00		NIST
Inp	514.00		NIST
Inp	520.00		NIST
Inp	511.00		NIST
Inp	527.00		NIST
Inp	528.00		NIST
Inp	529.00		NIST
Inp	515.00		NIST
Inp	519.00		NIST
Inp	515.00		NIST
Inp	515.00		NIST
Inp	531.00		NIST
Inp	515.00		NIST
Inp	512.00		NIST
Inp	515.00		NIST
Inp	515.00		NIST
Inp	504.00		NIST
Inp	510.00		NIST
Inp	527.00		NIST
Inp	530.00		NIST
Inp	524.00		NIST
Inp	524.00		NIST
Inp	515.00		NIST
Inp	512.70		NIST
Inp	531.00		NIST
Inp	511.00		NIST
Ip	[905.00; 953.00]
Ip	937.20		NIST
Ip	948.00		NIST
Ip	946.00		NIST
Ip	935.70		NIST
Ip	932.62		NIST
Ip	926.65		NIST
Ip	933.00		NIST
Ip	933.00		NIST
Ip	914.00		NIST
Ip	925.00		NIST
Ip	931.00		NIST
Ip	948.00		NIST
Ip	Outlier 905.00		NIST
Ip	937.20		NIST
Ip	936.00		NIST
Ip	927.00		NIST
Ip	933.00		NIST
Ip	953.00		NIST
Ip	944.00		NIST
Ip	932.00		NIST
Ip	937.00		NIST
Ip	944.00		NIST
Ip	933.00		NIST
Ip	919.00		NIST
Ip	925.00		NIST
Ip	928.00		NIST
Ip	912.00		NIST
Ip	927.00		NIST
Ip	933.00		NIST
Ip	914.00		NIST
Ip	917.00		NIST
Ip	933.00		NIST
Ip	948.00		NIST
S°liquid	174.50	J/mol×K	NIST
Tboil	[312.75; 314.95]	K
Tboil	313.00	K	KDB
Tboil	312.75	K	NCMS SOLV-DB
Tboil	312.93 ± 0.20	K	NIST
Tboil	313.00	K	NIST
Tboil	312.92 ± 0.07	K	NIST
Tboil	313.30 ± 0.30	K	NIST
Tboil	312.95 ± 0.50	K	NIST
Tboil	313.15 ± 1.00	K	NIST
Tboil	313.20 ± 0.50	K	NIST
Tboil	313.20 ± 1.00	K	NIST
Tboil	313.35 ± 0.20	K	NIST
Tboil	312.95 ± 0.30	K	NIST
Tboil	Outlier 314.70 ± 0.50	K	NIST
Tboil	Outlier 314.95 ± 0.50	K	NIST
Tc	[508.00; 510.00]	K
Tc	508.00	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 10 Compiled value
Tc	510.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	510.00	K	KDB
Tc	508.00 ± 0.20	K	NIST
Tc	510.00	K	NIST
Tfus	[176.00; 198.06]	K
Tfus	178.10	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	178.01	K	KDB
Tfus	177.62	K	Aq. Solubility Prediction
Tfus	178.23	K	NCMS SOLV-DB
Tfus	Outlier 198.06 ± 0.40	K	NIST
Tfus	176.00 ± 1.50	K	NIST
Tfus	177.00 ± 2.00	K	NIST
Tfus	176.65 ± 0.40	K	NIST
Vc	0.193	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Zra	0.26		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[95.72; 129.30]	J/mol×K	[180.00; 303.20]
Cp,liquid	96.88	J/mol×K	180.00	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	96.50	J/mol×K	190.00	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	96.16	J/mol×K	200.00	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	95.90	J/mol×K	210.00	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	95.74	J/mol×K	220.00	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	95.72	J/mol×K	230.00	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	95.88	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	96.25	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	96.86	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	97.76	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	98.11	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	98.97	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	100.50	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	100.50	J/mol×K	292.50	NIST
Cp,liquid	100.80	J/mol×K	292.50	NIST
Cp,liquid	129.30	J/mol×K	298.00	NIST
Cp,liquid	100.00	J/mol×K	298.00	NIST
Cp,liquid	100.00	J/mol×K	298.10	NIST
Cp,liquid	102.10	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	102.30	J/mol×K	298.15	NIST
Cp,liquid	102.50	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	105.50	J/mol×K	303.20	NIST
η	0.0004043	Pa×s	298.15	NCMS SOLV-DB
ΔfusH	[6.16; 6.16]	kJ/mol	[178.20; 178.22]
ΔfusH	6.16	kJ/mol	178.20	NIST
ΔfusH	6.16	kJ/mol	178.20	NIST
ΔfusH	6.16	kJ/mol	178.22	NIST
ΔvapH	[28.06; 30.30]	kJ/mol	[249.00; 347.00]
ΔvapH	29.40	kJ/mol	249.00	NIST
ΔvapH	30.20	kJ/mol	273.00	NIST
ΔvapH	30.30	kJ/mol	287.50	NIST
ΔvapH	29.20	kJ/mol	308.00	NIST
ΔvapH	28.06	kJ/mol	313.00	NIST
ΔvapH	29.00	kJ/mol	347.00	NIST
Pvap	[34.66; 197.94]	kPa	[285.89; 333.15]
Pvap	34.66	kPa	285.89	Limiting activity coefficient measurements in binary mixtures of dichloromethane and 1-alkanols (C1 - C4)
Pvap	37.10	kPa	287.00	Effect of Dissolved Poly(lactic acid) on the Solubility of CO2, N2, and He Gases in Dichloromethane
Pvap	37.33	kPa	287.58	Limiting activity coefficient measurements in binary mixtures of dichloromethane and 1-alkanols (C1 - C4)
Pvap	41.33	kPa	289.94	Limiting activity coefficient measurements in binary mixtures of dichloromethane and 1-alkanols (C1 - C4)
Pvap	45.70	kPa	291.90	Effect of Dissolved Poly(lactic acid) on the Solubility of CO2, N2, and He Gases in Dichloromethane
Pvap	45.33	kPa	292.12	Limiting activity coefficient measurements in binary mixtures of dichloromethane and 1-alkanols (C1 - C4)
Pvap	49.33	kPa	294.15	Limiting activity coefficient measurements in binary mixtures of dichloromethane and 1-alkanols (C1 - C4)
Pvap	53.33	kPa	296.05	Limiting activity coefficient measurements in binary mixtures of dichloromethane and 1-alkanols (C1 - C4)
Pvap	55.90	kPa	296.80	Effect of Dissolved Poly(lactic acid) on the Solubility of CO2, N2, and He Gases in Dichloromethane
Pvap	58.00	kPa	298.15	NCMS SOLV-DB
Pvap	58.66	kPa	298.41	Limiting activity coefficient measurements in binary mixtures of dichloromethane and 1-alkanols (C1 - C4)
Pvap	63.99	kPa	300.61	Limiting activity coefficient measurements in binary mixtures of dichloromethane and 1-alkanols (C1 - C4)
Pvap	67.40	kPa	301.80	Effect of Dissolved Poly(lactic acid) on the Solubility of CO2, N2, and He Gases in Dichloromethane
Pvap	69.33	kPa	302.67	Limiting activity coefficient measurements in binary mixtures of dichloromethane and 1-alkanols (C1 - C4)
Pvap	70.49	kPa	303.15	Total Vapor Pressure Measurements for 2-Ethoxyethanol with Carbon Tetrachloride, Chloroform, and Dichloromethane at 303.15 K
Pvap	74.66	kPa	304.61	Limiting activity coefficient measurements in binary mixtures of dichloromethane and 1-alkanols (C1 - C4)
Pvap	79.99	kPa	306.43	Limiting activity coefficient measurements in binary mixtures of dichloromethane and 1-alkanols (C1 - C4)
Pvap	85.33	kPa	308.17	Limiting activity coefficient measurements in binary mixtures of dichloromethane and 1-alkanols (C1 - C4)
Pvap	90.66	kPa	309.82	Limiting activity coefficient measurements in binary mixtures of dichloromethane and 1-alkanols (C1 - C4)
Pvap	95.99	kPa	311.39	Limiting activity coefficient measurements in binary mixtures of dichloromethane and 1-alkanols (C1 - C4)
Pvap	197.94	kPa	333.15	Vapor Liquid Equilibrium and Excess Enthalpy Data for Systems Containing N,N-Dimethylacetamide
n0	[1.42100; 1.44590]		[283.15; 298.15]
n0	1.43050		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	1.42760		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	1.44590		293.15	Phase Equilibria of Water + Furfural and Dichloromethane + n-Hexane
n0	1.42370		293.15	Solubilities of Some Phosphaspirocyclic Compounds in Selected Solvents
n0	1.42370		293.15	Solubilities of Phosphorus-Containing Compounds in Selected Solvents
n0	1.42510		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	1.42190		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	1.42100		298.15	NCMS SOLV-DB
ρl	[1307.51; 1334.81]	kg/m3	[288.15; 303.15]
ρl	1334.81	kg/m3	288.15	Volumetric properties of dichloromethane with aniline or nitrobenzene at different temperatures: A theoretical and experimental study
ρl	1334.08	kg/m3	288.15	Volumetric properties of binary liquid mixtures: Application of the Prigogine Flory Patterson theory to excess molar volumes of dichloromethane with benzene or toluene
ρl	1325.67	kg/m3	293.15	Volumetric properties of dichloromethane with aniline or nitrobenzene at different temperatures: A theoretical and experimental study
ρl	1325.79	kg/m3	293.15	Volumetric properties of binary liquid mixtures: Application of the Prigogine Flory Patterson theory to excess molar volumes of dichloromethane with benzene or toluene
ρl	1327.00	kg/m3	293.15	Interfacial Properties, Densities, and Contact Angles of Task Specific Ionic Liquids
ρl	1317.00	kg/m3	298.00	KDB
ρl	1316.58	kg/m3	298.15	Volumetric properties of dichloromethane with aniline or nitrobenzene at different temperatures: A theoretical and experimental study
ρl	1316.75	kg/m3	298.15	Volumetric properties of binary liquid mixtures: Application of the Prigogine Flory Patterson theory to excess molar volumes of dichloromethane with benzene or toluene
ρl	1307.90	kg/m3	303.15	Volumetric properties of dichloromethane with aniline or nitrobenzene at different temperatures: A theoretical and experimental study
ρl	1307.51	kg/m3	303.15	Volumetric properties of binary liquid mixtures: Application of the Prigogine Flory Patterson theory to excess molar volumes of dichloromethane with benzene or toluene
ρl	1307.60	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
γ	[0.03; 0.03]	N/m	[293.20; 298.15]
γ	0.03	N/m	293.20	KDB
γ	0.03	N/m	298.15	NCMS SOLV-DB

Pressure Dependent Properties

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[50.85; 91.30]	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			1.91735e+01
Coefficient B			1.36844e+02
Coefficient C			-9.51299e+01
Coefficient D			2.60311e+01
Coefficient E			-1.19405e-01
Reference			Chase, 1998
Comment			F=-106.9338, G=256.0144, H=-95.52114; Data last reviewed in December, 1968
Temperature range, min.			298.00
Temperature range, max.			1200.00
Cp,gas	50.85	J/mol×K	298.00	Calculated Property
Cp,gas	59.47	J/mol×K	398.22	Calculated Property
Cp,gas	66.49	J/mol×K	498.44	Calculated Property
Cp,gas	72.26	J/mol×K	598.67	Calculated Property
Cp,gas	76.99	J/mol×K	698.89	Calculated Property
Cp,gas	80.88	J/mol×K	799.11	Calculated Property
Cp,gas	84.09	J/mol×K	899.33	Calculated Property
Cp,gas	86.79	J/mol×K	999.56	Calculated Property
Cp,gas	89.14	J/mol×K	1099.78	Calculated Property
Cp,gas	91.30	J/mol×K	1200.00	Calculated Property
Cp,gas	[91.11; 107.17]	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			9.51299e+01
Coefficient B			6.72172e+00
Coefficient C			-1.28820e+00
Coefficient D			8.56460e-02
Coefficient E			-1.49389e+01
Reference			Chase, 1998
Comment			F=-157.3506, G=340.5412, H=-95.52114; Data last reviewed in December, 1968
Temperature range, min.			1200.00
Temperature range, max.			6000.00
Cp,gas	91.11	J/mol×K	1200.00	Calculated Property
Cp,gas	98.38	J/mol×K	1733.33	Calculated Property
Cp,gas	101.84	J/mol×K	2266.67	Calculated Property
Cp,gas	103.83	J/mol×K	2800.00	Calculated Property
Cp,gas	105.05	J/mol×K	3333.33	Calculated Property
Cp,gas	105.81	J/mol×K	3866.67	Calculated Property
Cp,gas	106.29	J/mol×K	4400.00	Calculated Property
Cp,gas	106.61	J/mol×K	4933.33	Calculated Property
Cp,gas	106.87	J/mol×K	5466.67	Calculated Property
Cp,gas	107.17	J/mol×K	6000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 6037.79]	kPa	[229.18; 510.00]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.43555e+01
Coefficient B			-2.65134e+03
Coefficient C			-4.07080e+01
Temperature range, min.			229.18
Temperature range, max.			510.00
Pvap	1.33	kPa	229.18	Calculated Property
Pvap	9.84	kPa	260.38	Calculated Property
Pvap	44.13	kPa	291.58	Calculated Property
Pvap	142.05	kPa	322.79	Calculated Property
Pvap	362.24	kPa	353.99	Calculated Property
Pvap	779.68	kPa	385.19	Calculated Property
Pvap	1477.51	kPa	416.39	Calculated Property
Pvap	2538.44	kPa	447.60	Calculated Property
Pvap	4037.60	kPa	478.80	Calculated Property
Pvap	6037.79	kPa	510.00	Calculated Property
Pvap	[7.05e-03; 6143.24]	kPa	[178.01; 510.00]	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			8.08779e+01
Coefficient B			-6.03061e+03
Coefficient C			-1.00863e+01
Coefficient D			9.81251e-06
Coefficient E			0.00000e+00
Temperature range, min.			178.01
Temperature range, max.			510.00
Pvap	7.05e-03	kPa	178.01	Calculated Property
Pvap	0.41	kPa	214.90	Calculated Property
Pvap	5.96	kPa	251.79	Calculated Property
Pvap	38.97	kPa	288.67	Calculated Property
Pvap	154.35	kPa	325.56	Calculated Property
Pvap	441.82	kPa	362.45	Calculated Property
Pvap	1018.41	kPa	399.34	Calculated Property
Pvap	2026.99	kPa	436.22	Calculated Property
Pvap	3650.30	kPa	473.11	Calculated Property
Pvap	6143.24	kPa	510.00	Calculated Property
Pvap	[70.52; 102.12]	kPa	[303.14; 313.14]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.37539e+01
Coefficient B			-2.34142e+03
Coefficient C			-5.66230e+01
Reference			Mueller and Ignatowski, 1960, 2
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			303.14
Temperature range, max.			313.14
Pvap	70.52	kPa	303.14	Calculated Property
Pvap	73.59	kPa	304.25	Calculated Property
Pvap	76.76	kPa	305.36	Calculated Property
Pvap	80.04	kPa	306.47	Calculated Property
Pvap	83.44	kPa	307.58	Calculated Property
Pvap	86.94	kPa	308.70	Calculated Property
Pvap	90.56	kPa	309.81	Calculated Property
Pvap	94.29	kPa	310.92	Calculated Property
Pvap	98.14	kPa	312.03	Calculated Property
Pvap	102.12	kPa	313.14	Calculated Property
Pvap	[1.96; 100.12]	kPa	[233.00; 313.00]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.50518e+01
Coefficient B			-3.05557e+03
Coefficient C			-2.04740e+01
Reference			Ganeff and Jungers, 1948
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			233.00
Temperature range, max.			313.00
Pvap	1.96	kPa	233.00	Calculated Property
Pvap	3.50	kPa	241.89	Calculated Property
Pvap	5.96	kPa	250.78	Calculated Property
Pvap	9.75	kPa	259.67	Calculated Property
Pvap	15.41	kPa	268.56	Calculated Property
Pvap	23.60	kPa	277.44	Calculated Property
Pvap	35.11	kPa	286.33	Calculated Property
Pvap	50.93	kPa	295.22	Calculated Property
Pvap	72.17	kPa	304.11	Calculated Property
Pvap	100.12	kPa	313.00	Calculated Property
Pvap	[70.52; 102.12]	kPa	[303.14; 313.14]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.37539e+01
Coefficient B			-2.34142e+03
Coefficient C			-5.66230e+01
Reference			Mueller and Ignatowski, 1960
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			303.14
Temperature range, max.			313.14
Pvap	70.52	kPa	303.14	Calculated Property
Pvap	73.59	kPa	304.25	Calculated Property
Pvap	76.76	kPa	305.36	Calculated Property
Pvap	80.04	kPa	306.47	Calculated Property
Pvap	83.44	kPa	307.58	Calculated Property
Pvap	86.94	kPa	308.70	Calculated Property
Pvap	90.56	kPa	309.81	Calculated Property
Pvap	94.29	kPa	310.92	Calculated Property
Pvap	98.14	kPa	312.03	Calculated Property
Pvap	102.12	kPa	313.14	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 0.03]	N/m	[178.15; 313.15]	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			6.54825e-02
Coefficient B			-1.28400e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			178.15
Temperature range, max.			313.15
γ	0.04	N/m	178.15	Calculated Property
γ	0.04	N/m	193.15	Calculated Property
γ	0.04	N/m	208.15	Calculated Property
γ	0.04	N/m	223.15	Calculated Property
γ	0.03	N/m	238.15	Calculated Property
γ	0.03	N/m	253.15	Calculated Property
γ	0.03	N/m	268.15	Calculated Property
γ	0.03	N/m	283.15	Calculated Property
γ	0.03	N/m	298.15	Calculated Property
γ	0.03	N/m	313.15	Calculated Property

Similar Compounds

Find more compounds similar to Methylene chloride.

Mixtures

• Methylene chloride + Methyl Alcohol
• Methylene chloride + Ethanol
• 1-Propanol + Methylene chloride
• Methylene chloride + 1-Butanol
• Carbon dioxide + Methylene chloride + Eugenol
• Benzene + Methylene chloride
• Toluene + Methylene chloride
• Methylene chloride + Propanoic acid + Water
• Methylene chloride + Water
• Methylene chloride + Ethane, 1,2-dichloro- + Water
• Aniline + Methylene chloride
• Benzene, nitro- + Methylene chloride
• Methylene chloride + Acetic acid, methyl ester
• Methylene chloride + Ethyl Acetate
• Methylene chloride + Acetic acid, propyl ester
• Methylene chloride + Acetic acid, butyl ester
• Methylene chloride + 1-Butanol, 3-methyl-, acetate
• 1,3-Dioxolane + Methylene chloride + Acetic acid, methyl ester
• 1,3-Dioxolane + Methylene chloride + Ethyl Acetate
• 1,3-Dioxolane + Methylene chloride + Acetic acid, propyl ester

Find more mixtures with Methylene chloride.

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.
• Co-solvent effects in LLE of 1-hydroxyethyl-3-methylimidazolium based ionic liquids + 2-propanol + dichloromethane or 1,2-dichloroethane
• A simple apparatus for data solubility determination
• Phase behavior of the poly(vinyl pyrrolidone) + dichloromethane + supercritical carbon dioxide system
• 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
• Solubility of 1, 3, 2-dioxaphosphorinane-5,5-dimethyl -2- (2,4,6-tribromophenoxy)-2-oxide in selected solvents
• Liquid-vapor equilibrium data of CO2+ dichloromethane + medroxyprogesterone system
• 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
• Determination and correlation of liquid-liquid equilibrium data for the dichloromethane + water + N, N-dimethylacetamide + NaCl system
• Limiting activity coefficient measurements in binary mixtures of dichloromethane and 1-alkanols (C1 - C4)
• High-pressure phase equilibrium data for carbon dioxide p dichloromethane p acetone and carbon dioxide p dichloromethane p acetone p N-acetylcysteine (NAC)
• Measurement of activity coefficients at infinite dilution in 1-hexadecyl-3-methylimidazolium tetrafluoroborate ionic liquid
• Volumetric properties of dichloromethane with aniline or nitrobenzene at different temperatures: A theoretical and experimental study
• Binodal curve measurements for (water + propionic acid + dichloromethane) ternary system by cloud point method
• Volumetric properties of binary liquid mixtures: Application of the Prigogine Flory Patterson theory to excess molar volumes of dichloromethane with benzene or toluene
• Interactions of volatile organic compounds with the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
• Excess properties of binary mixtures containing 1-hexyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide ionic liquid and polar organic compounds
• 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
• (Liquid + liquid) equilibria of quaternary systems containing water, phosphoric acid, dichloromethane and 1,2-dichloroethane
• 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
• Salting-out effect on the (liquid + liquid) equilibrium for the ternary systems (water + phosphoric acid + dichloromethane or 1,2-dichloroethane)
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-butyl-3-methylimidazolium methyl sulfate
• (Solid + liquid) phase equilibria of tetraphenyl piperazine-1,4-diyldiphosphonate in pure solvents
• Activity coefficients at infinite dilution of organic solutes in methylphosphonate based ionic liquids using gas-liquid chromatography
• Phase equilibrium data for ternary (carbon dioxide + dichloromethane + eugenol) and quaternary systems (carbon dioxide + dichloromethane + eugenol + poly-.epsilon.-caprolactone)
• Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-hexyl-2,3-dimethylimidazolium bis(trifluoromethylsulfonyl)imide
• 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
• Studies on liquid liquid interactions of some ternary mixtures by density, viscosity, ultrasonic speed and refractive index measurements
• Determination of the solubility, dissolution enthalpy and entropy of 3-pentadecylphenyl acrylate in different organic solvents
• Examination of hydrogen-bonding interactions between dissolved solutes and alkylbenzene solvents based on Abraham model correlations derived from measured enthalpies of solvation
• 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
• 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
• Determination and Correlation of Solubility of N-tertbutylacrylamide in Seven Different Solvents at Temperatures between (279.15 and 353.15) K
• Effect of Dissolved Poly(lactic acid) on the Solubility of CO2, N2, and He Gases in Dichloromethane
• Solubility Measurement and Correlation of (+)-Biotin Intermediate Lactone in Different Organic Solvents from (287.15 to 323.75) K
• Equilibrium Study on the Extraction of Levulinic Acid from Aqueous Solution with Aliquat 336 Dissolved in Different Diluents: Solvent s Polarity Effect and Column Design
• 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
• Solvent Polarity Effect when Amberlite-LA2 Is Used in the Extraction of Picric Acid
• Vapor Liquid Equilibrium and Excess Enthalpy Data for Systems Containing N,N-Dimethylacetamide
• Measurements and Thermodynamic Models for the Separation of 2-Methoxyethanol and Water Azeotropic Mixtures via Different Solvents
• 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 the Dissolution Equilibria of o-Iodoaniline and p-Iodoaniline in Pure Solvents
• Solution Thermodynamics of Benzotriazole in Different Pure Solvents
• Determination of Activity Coefficients at Infinite Dilution of Organic Solutes in the Ionic Liquid 1-(2-Hydroxyethyl)-3-methylimidazolium Nonafluoro-1-butanesulfonate Using Gas-Liquid Chromatography
• Solubility of Toltrazuril and the Effect of a Cosolvent
• Physico-Chemical Properties of LiFSI Solutions I. LiFSI with Valeronitrile, Dichloromethane, 1,2-Dichloroethane, and 1,2-Dichlorobenzene
• Determination of Activity Coefficients at Infinite Dilution of Solutes in N,N'-Di(2-ethylhexyl)isobutyramide Using Inverse Gas-Liquid Chromatography
• High Pressure Phase Equilibrium Data for the Ternary System Containing Carbon Dioxide, Dichloromethane, and epsilon-Caprolactone
• Solid-Liquid Equilibrium of Azacyclotridecan-2-one in 15 Pure Solvents from T = 273.15 to 323.15 K: Experimental Determination and Thermodynamic Modeling
• Measurement and Correlation of the Solubility of 2-Cyanoacetamide in 14 Pure Solvents and the Mixing Properties of Solutions
• Thermodynamic Studies of Solubility for Naphthalene in 12 Solvents from 279 to 330 K
• Solubility Measurement and Correlation of 2-Oxindole in 12 Pure Organic Solvents
• Solubility Determination, Modeling, and Thermodynamic Dissolution Properties of Benzenesulfonamide in 16 Neat Solvents from 273.15 to 324.45 K
• Solubility, Solubility Modeling, and Antisolvent Precipitation of 1,3-Bis(9-carbazolyl)benzene in Organic Solvents
• Solubility Measurement and Thermodynamic Modeling for o-Toluenesulfonamide in 16 Solvents from T = 273.15 to 323.85 K
• Phase Equilibria of Water + Furfural and Dichloromethane + n-Hexane
• 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
• High Pressure Phase Equilibria of the Related Substances in the Limonene Oxidation in Supercritical CO2
• 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
• Phase Behavior, Densities, and Isothermal Compressibility of the CO2 + Ethanol + Dichloromethane Ternary System in Different Phase Regions
• Phase Separation in Binary Mixtures Containing Linear Perfluoroalkanes
• High-Pressure Vapor-Liquid Equilbria of Some Carbon Dioxide + Organic Binary Systems
• Solubility of Imidazoles, Benzimidazoles, and Phenylimidazoles in Dichloromethane, 1-Chlorobutane, Toluene, and 2-Nitrotoluene
• Solubility of Cefazolin Sodium Pentahydrate in Different Solvents between 275 K and 310 K
• 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
• Solubilities of Some Phosphaspirocyclic Compounds in Selected Solvents
• Activity Coefficients at Infinite Dilution of Polar Solutes in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Solubility of Acephate in Different Solvents from (292.90 to 327.60) K
• Densities and Excess Molar Volumes for Binary Mixtures of Ionic Liquid 1-Ethyl-3-methylimidazolium Ethylsulfate with Solvents
• 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
• Solubilities of (a,Z)-2-Amino-a-(methoxyimino)-4-thiazoleethanethioic Acid S-2-Benzothiazolyl Ester in Different Pure Solvents and Binary Mixtures of Tetrahydrofuran + Dichloromethane or 1,2-Dichloroethane
• Solubilities of Phenylphosphinic Acid, Methylphenylphosphinic Acid, Hexachlorocyclotriphosphazene, and Hexaphenoxycyclotriphosphazene in Selected Solvents
• 1-Ethyl-3-methylimidazolium Ethylsulfate in Water, Acetonitrile, and Dichloromethane: Molar Conductivities and Association Constants
• 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
• 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
• Determination of Gas Concentrations in Liquids by Nuclear Magnetic Resonance: Hydrogen 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
• 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 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
• Measurement and Correlation of Solubilities of Indole-2-carboxylic Acid in Ten Different Pure Solvents from (278.15 to 360.15) K
• Determination and Correlation of Liquid Liquid Equilibrium Data for the Ternary Dichloromethane + Water + N,N-Dimethylacetamide System
• 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
• 4-Amino-3,6-dichloropyridazine Solubility Measurement and Correlation in Seven Pure Organic Solvents from (278.15 to 333.15) K
• Solubility and Thermodynamic Functions of Isatin in Pure Solvents
• Measurement and Correlation of Solubility of Tetraphenyl Piperazine-1,4-diyldiphosphonate in Mixed Solvents
• Solubility of Simvastatin and Lovastatin in Mixtures of Dichloromethane and Supercritical Carbon Dioxide
• Solubilities of Betulin in Fourteen Organic Solvents at Different Temperatures
• Solubility of Imidacloprid in Different Solvents
• Henry s Law Constants for Fragrance and Organic Solvent Compounds in Aqueous Industrial Surfactants
• 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
• Solubilities of Adefovir Dipivoxil in Different Binary Solvents at 298.15 K
• Liquid Liquid Equilibria for the Ternary Systems Water + n-Pentanoic Acid with n-Heptane or Dichloromethane at 298.2 K
• Solubility of Rifapentine in Different Organic Solvents
• Ion Pair Formation of Alkylimidazolium Ionic Liquids in Dichloromethane
• Gas Solubilities (CO2, O2, Ar, N2, H2, and He) in Liquid Chlorinated Methanes
• 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
• Conductivities of Binary Mixtures of Ionic Liquids with Polar Solvents
• Solubility of Enrofloxacin Sodium in Various Solvents at Various Temperatures
• 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
• Solubility of Valsartan in Different Organic Solvents and Ethanol + Water Binary Mixtures from (278.15 to 313.15) K
• Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
• Interfacial Properties, Densities, and Contact Angles of Task Specific Ionic Liquids
• Solubility of Ofloxacin in 1,2-Dichloromethane, Chloroform, Carbon Tetrachloride, and Water from (293.15 to 313.15) K
• Stability of Ion Pairs of Bis(trifluoromethanesulfonyl)amide-Based Ionic Liquids in Dichloromethane
• Activity Coefficients at Infinite Dilution of Polar Solutes in 1-(2-Hydroxyethyl)-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Solubilities of (?,Z)-2-Amino-?-(methoxyimino)-4-thiazole-ethanethioic Acid S-2-Benzothiazolyl Ester in Pure Solvents and a Mixture of Acetonitrile and Dichloromethane
• Study of Ether-, Alcohol-, or Cyano-Functionalized Ionic Liquids Using Inverse Gas Chromatography
• 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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