Chemical Properties of 2-Pentanone (CAS 107-87-9)

InChI

InChI=1S/C5H10O/c1-3-4-5(2)6/h3-4H2,1-2H3

InChI Key

XNLICIUVMPYHGG-UHFFFAOYSA-N

Formula

C5H10O

SMILES

CCCC(C)=O

Molecular Weight¹

86.13

CAS

107-87-9

Other Names

• Ethyl acetone
• MPK
• Metylopropyloketon
• NSC 5350
• Pentanone-2
• UN 1249
• methyl n-propyl ketone
• methyl propyl ketone
• n-C3H7COCH3
• n-Propyl methyl ketone
• pentan-2-one
• propyl methyl ketone

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• T_ig : Autoignition Temperature (K).
• BasG : Gas basicity (kJ/mol).
• Δ_cH°_gas : Standard gas enthalpy of combustion (kJ/mol).
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• ε_r : Dielectric Constant (Relative permittivity).
• T_flash,cc : Flash Point (Closed Cup Method) (K).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• 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_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_c : Critical density (kg/m³).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I_p : Polar retention indices.
• 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 : Gas thermal conductivity (W/m×K).
• λ_liquid : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• U_Qi : UNIQUAC Qi Parameter.
• U_Ri : UNIQUAC Ri Parameter.
• V_c : Critical Volume (m³/kmol).
• Z_c : Critical Compressibility.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	[0.3396; 0.3460]
ω	0.3396		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.3460		ChemSep v8.3 pure component data Compiled value
ω	0.3460		KDB
PAff	832.70	kJ/mol	NIST
Tig	725.15	K	NCMS SOLV-DB
BasG	800.90	kJ/mol	NIST
ΔcH°gas	-3156.00	kJ/mol	NIST
ΔcH°liquid	-3099.40 ± 0.80	kJ/mol	NIST
μ	[2.50; 2.72]	debye
μ	2.72	debye	ChemSep v8.3 pure component data Compiled value
μ	2.50	debye	KDB
εr	13.60		NCMS SOLV-DB
Tflash,cc	280.15	K	NCMS SOLV-DB
ΔfG°	[-138.40; -137.20]	kJ/mol
ΔfG°	-138.40	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	-137.20	kJ/mol	KDB
ΔfH°gas	[-259.20; -258.80]	kJ/mol
ΔfH°gas	-259.20	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-258.80	kJ/mol	KDB
ΔfH°gas	-259.10 ± 1.10	kJ/mol	NIST
ΔfH°liquid	-297.30 ± 1.10	kJ/mol	NIST
ΔfusH°	10.30	kJ/mol	Joback Calculated Property
ΔvapH°	[38.30; 38.46]	kJ/mol
ΔvapH°	38.41	kJ/mol	NCMS SOLV-DB
ΔvapH°	38.46	kJ/mol	NIST
ΔvapH°	38.43	kJ/mol	NIST
ΔvapH°	38.40	kJ/mol	NIST
ΔvapH°	Outlier 38.30 ± 0.30	kJ/mol	NIST
ΔvapH°	38.40	kJ/mol	NIST
IE	[9.28; 9.47]	eV
IE	9.38 ± 0.06	eV	NIST
IE	Outlier 9.28 ± 0.02	eV	NIST
IE	9.38 ± 0.01	eV	NIST
IE	9.40 ± 0.01	eV	NIST
IE	9.37 ± 0.02	eV	NIST
IE	9.39 ± 0.02	eV	NIST
IE	9.47 ± 0.03	eV	NIST
IE	9.46	eV	NIST
IE	9.44	eV	NIST
log10WS	[-0.19; -0.19]
log10WS	-0.19		Aq. Solubility Prediction
log10WS	-0.19		Estimated Solubility
logPoct/wat	0.910		NCMS SOLV-DB
McVol	82.880	ml/mol	McGowan Calculated Property
NFPA Fire	[%!d(float64=3); %!d(float64=3)]
NFPA Fire	3		KDB
NFPA Fire	3		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	[3672.00; 3890.00]	kPa
Pc	3683.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Pc	3672.00	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	3690.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	3694.00	kPa	KDB
Pc	3694.00 ± 20.00	kPa	NIST
Pc	Outlier 3890.00 ± 48.30	kPa	NIST
Ptriple	7.52e-04	kPa	ChemSep v8.3 pure component data Compiled value
ρc	285.96 ± 7.75	kg/m3	NIST
Inp	[623.00; 716.00]
Inp	663.30		NIST
Inp	667.09		NIST
Inp	666.82		NIST
Inp	666.11		NIST
Inp	665.42		NIST
Inp	666.63		NIST
Inp	667.23		NIST
Inp	668.17		NIST
Inp	668.33		NIST
Inp	669.68		NIST
Inp	670.44		NIST
Inp	672.02		NIST
Inp	674.86		NIST
Inp	693.14		NIST
Inp	692.22		NIST
Inp	691.63		NIST
Inp	691.20		NIST
Inp	690.53		NIST
Inp	691.40		NIST
Inp	691.57		NIST
Inp	691.79		NIST
Inp	692.92		NIST
Inp	694.09		NIST
Inp	696.34		NIST
Inp	697.44		NIST
Inp	672.20		NIST
Inp	673.99		NIST
Inp	671.87		NIST
Inp	652.20		NIST
Inp	638.93		NIST
Inp	666.90		NIST
Inp	665.40		NIST
Inp	665.40		NIST
Inp	665.40		NIST
Inp	665.40		NIST
Inp	665.69		NIST
Inp	666.07		NIST
Inp	Outlier 631.00		NIST
Inp	636.00		NIST
Inp	667.00		NIST
Inp	665.00		NIST
Inp	666.00		NIST
Inp	666.00		NIST
Inp	674.00		NIST
Inp	676.00		NIST
Inp	672.00		NIST
Inp	673.00		NIST
Inp	649.00		NIST
Inp	669.20		NIST
Inp	675.30		NIST
Inp	663.00		NIST
Inp	682.00		NIST
Inp	Outlier 629.60		NIST
Inp	688.50		NIST
Inp	690.00		NIST
Inp	691.20		NIST
Inp	685.60		NIST
Inp	685.00		NIST
Inp	668.00		NIST
Inp	668.00		NIST
Inp	672.00		NIST
Inp	675.00		NIST
Inp	671.00		NIST
Inp	Outlier 630.00		NIST
Inp	636.00		NIST
Inp	Outlier 624.00		NIST
Inp	Outlier 627.00		NIST
Inp	Outlier 626.00		NIST
Inp	Outlier 631.00		NIST
Inp	671.00		NIST
Inp	666.00		NIST
Inp	646.00		NIST
Inp	653.00		NIST
Inp	644.00		NIST
Inp	642.00		NIST
Inp	Outlier 634.80		NIST
Inp	673.00		NIST
Inp	674.00		NIST
Inp	Outlier 624.00		NIST
Inp	Outlier 623.00		NIST
Inp	642.00		NIST
Inp	654.00		NIST
Inp	644.00		NIST
Inp	638.00		NIST
Inp	687.00		NIST
Inp	703.00		NIST
Inp	705.00		NIST
Inp	666.00		NIST
Inp	692.00		NIST
Inp	697.00		NIST
Inp	664.80		NIST
Inp	680.00		NIST
Inp	686.00		NIST
Inp	695.00		NIST
Inp	651.00		NIST
Inp	699.00		NIST
Inp	683.00		NIST
Inp	689.00		NIST
Inp	685.00		NIST
Inp	710.00		NIST
Inp	673.90		NIST
Inp	653.00		NIST
Inp	689.00		NIST
Inp	681.80		NIST
Inp	692.00		NIST
Inp	653.00		NIST
Inp	653.00		NIST
Inp	680.00		NIST
Inp	680.00		NIST
Inp	692.00		NIST
Inp	673.00		NIST
Inp	653.00		NIST
Inp	653.00		NIST
Inp	693.00		NIST
Inp	Outlier 715.00		NIST
Inp	680.00		NIST
Inp	698.00		NIST
Inp	684.00		NIST
Inp	682.00		NIST
Inp	684.00		NIST
Inp	689.00		NIST
Inp	Outlier 715.00		NIST
Inp	Outlier 715.00		NIST
Inp	666.00		NIST
Inp	682.00		NIST
Inp	Outlier 630.00		NIST
Inp	666.00		NIST
Inp	700.00		NIST
Inp	663.00		NIST
Inp	664.00		NIST
Inp	661.00		NIST
Inp	662.00		NIST
Inp	662.00		NIST
Inp	662.00		NIST
Inp	645.00		NIST
Inp	686.00		NIST
Inp	Outlier 711.00		NIST
Inp	700.00		NIST
Inp	680.00		NIST
Inp	Outlier 716.00		NIST
Inp	705.00		NIST
Inp	677.00		NIST
Inp	667.00		NIST
Inp	666.00		NIST
Inp	667.00		NIST
Inp	668.00		NIST
Inp	669.00		NIST
Inp	669.00		NIST
Inp	667.00		NIST
Inp	670.00		NIST
Inp	669.00		NIST
Inp	666.00		NIST
Inp	668.00		NIST
Inp	668.00		NIST
Inp	670.00		NIST
Inp	665.00		NIST
Inp	655.00		NIST
Inp	640.00		NIST
Inp	671.00		NIST
Inp	668.00		NIST
Inp	678.00		NIST
Inp	680.00		NIST
Inp	670.00		NIST
Inp	661.00		NIST
Inp	703.00		NIST
Inp	685.00		NIST
Inp	685.00		NIST
Inp	662.00		NIST
Inp	698.00		NIST
Inp	698.00		NIST
Inp	688.00		NIST
Inp	689.00		NIST
Inp	671.00		NIST
Inp	687.00		NIST
Inp	685.00		NIST
Inp	659.00		NIST
Inp	655.00		NIST
Inp	681.00		NIST
Inp	684.00		NIST
Inp	686.00		NIST
Inp	664.00		NIST
Inp	674.00		NIST
Inp	685.00		NIST
Inp	681.00		NIST
Inp	680.00		NIST
Inp	693.00		NIST
Inp	666.00		NIST
Inp	690.00		NIST
Inp	682.00		NIST
Inp	652.00		NIST
Inp	655.00		NIST
Inp	652.00		NIST
Inp	658.00		NIST
Inp	688.00		NIST
Inp	691.00		NIST
Inp	690.00		NIST
Inp	672.00		NIST
Inp	658.00		NIST
Inp	672.00		NIST
Inp	679.00		NIST
Inp	705.00		NIST
Inp	664.00		NIST
Inp	665.00		NIST
Inp	660.00		NIST
Inp	677.00		NIST
Inp	673.00		NIST
Inp	695.00		NIST
Inp	699.00		NIST
Inp	674.00		NIST
Inp	699.00		NIST
Inp	684.00		NIST
Inp	690.00		NIST
Inp	673.00		NIST
Inp	660.00		NIST
Inp	671.00		NIST
Inp	700.00		NIST
Inp	654.00		NIST
Inp	666.00		NIST
Inp	682.00		NIST
Inp	684.00		NIST
Inp	689.00		NIST
Inp	689.00		NIST
Inp	689.00		NIST
Inp	700.00		NIST
Inp	649.00		NIST
Inp	680.00		NIST
Inp	686.00		NIST
Inp	686.00		NIST
Inp	665.00		NIST
Inp	672.00		NIST
Inp	678.00		NIST
Inp	653.00		NIST
Inp	665.00		NIST
Inp	685.00		NIST
Inp	687.00		NIST
Inp	679.00		NIST
Inp	684.00		NIST
Inp	644.00		NIST
Inp	Outlier 629.00		NIST
Inp	663.00		NIST
Inp	684.00		NIST
Inp	669.00		NIST
Inp	670.00		NIST
Inp	676.00		NIST
Inp	663.00		NIST
Inp	663.00		NIST
Inp	669.00		NIST
Inp	680.00		NIST
Inp	658.00		NIST
Inp	672.00		NIST
Inp	664.00		NIST
Inp	666.00		NIST
Inp	674.00		NIST
Inp	639.00		NIST
Inp	680.00		NIST
Inp	686.00		NIST
Inp	705.00		NIST
Inp	663.30		NIST
Inp	666.63		NIST
Inp	670.44		NIST
Inp	691.63		NIST
Inp	691.79		NIST
Inp	672.20		NIST
Inp	666.90		NIST
Inp	665.69		NIST
Inp	665.00		NIST
Inp	672.00		NIST
Inp	663.00		NIST
Inp	691.20		NIST
Inp	Outlier 624.00		NIST
Inp	666.00		NIST
Inp	Outlier 634.80		NIST
Inp	642.00		NIST
Inp	695.00		NIST
Inp	690.00		NIST
Inp	654.00		NIST
Inp	689.00		NIST
Inp	653.00		NIST
Inp	684.00		NIST
Inp	669.00		NIST
Inp	667.00		NIST
Inp	668.00		NIST
Inp	640.00		NIST
Inp	671.00		NIST
Inp	661.00		NIST
Inp	698.00		NIST
Inp	687.00		NIST
Inp	681.00		NIST
Inp	682.00		NIST
Inp	688.00		NIST
Inp	660.00		NIST
Inp	680.00		NIST
Inp	Outlier 715.00		NIST
Inp	700.00		NIST
Inp	662.00		NIST
Ip	[938.00; 1025.00]
Ip	1003.89		NIST
Ip	1012.78		NIST
Ip	1022.25		NIST
Ip	1010.70		NIST
Ip	979.40		NIST
Ip	1003.89		NIST
Ip	1005.72		NIST
Ip	1007.52		NIST
Ip	1009.73		NIST
Ip	1011.09		NIST
Ip	1012.78		NIST
Ip	1014.87		NIST
Ip	1016.30		NIST
Ip	1018.39		NIST
Ip	1020.31		NIST
Ip	1022.25		NIST
Ip	1023.72		NIST
Ip	986.78		NIST
Ip	1015.63		NIST
Ip	1021.54		NIST
Ip	1010.70		NIST
Ip	996.20		NIST
Ip	1000.70		NIST
Ip	1005.60		NIST
Ip	990.20		NIST
Ip	979.40		NIST
Ip	992.60		NIST
Ip	994.60		NIST
Ip	979.00		NIST
Ip	996.00		NIST
Ip	974.00		NIST
Ip	978.00		NIST
Ip	969.00		NIST
Ip	990.00		NIST
Ip	998.00		NIST
Ip	969.00		NIST
Ip	997.60		NIST
Ip	983.00		NIST
Ip	968.00		NIST
Ip	945.00		NIST
Ip	971.00		NIST
Ip	978.00		NIST
Ip	1005.00		NIST
Ip	985.00		NIST
Ip	991.10		NIST
Ip	945.00		NIST
Ip	944.00		NIST
Ip	943.00		NIST
Ip	944.00		NIST
Ip	996.00		NIST
Ip	988.00		NIST
Ip	980.00		NIST
Ip	975.00		NIST
Ip	975.00		NIST
Ip	993.00		NIST
Ip	978.00		NIST
Ip	Outlier 938.00		NIST
Ip	977.00		NIST
Ip	Outlier 938.00		NIST
Ip	943.00		NIST
Ip	978.00		NIST
Ip	979.00		NIST
Ip	983.40		NIST
Ip	984.30		NIST
Ip	984.40		NIST
Ip	987.00		NIST
Ip	971.00		NIST
Ip	980.00		NIST
Ip	980.00		NIST
Ip	982.00		NIST
Ip	979.00		NIST
Ip	984.00		NIST
Ip	983.00		NIST
Ip	968.00		NIST
Ip	944.00		NIST
Ip	971.00		NIST
Ip	970.00		NIST
Ip	974.00		NIST
Ip	976.00		NIST
Ip	965.00		NIST
Ip	990.00		NIST
Ip	1001.00		NIST
Ip	981.00		NIST
Ip	971.00		NIST
Ip	984.00		NIST
Ip	982.00		NIST
Ip	972.00		NIST
Ip	970.00		NIST
Ip	992.00		NIST
Ip	1015.00		NIST
Ip	1018.00		NIST
Ip	983.00		NIST
Ip	990.00		NIST
Ip	Outlier 1025.00		NIST
Ip	980.00		NIST
Ip	992.00		NIST
Ip	960.00		NIST
Ip	975.00		NIST
Ip	969.00		NIST
Ip	957.00		NIST
Ip	969.00		NIST
Ip	975.00		NIST
Ip	Outlier 940.00		NIST
Ip	990.00		NIST
Ip	1000.00		NIST
Ip	989.00		NIST
Ip	971.00		NIST
Ip	976.00		NIST
Ip	966.00		NIST
Ip	Outlier 940.00		NIST
Ip	975.00		NIST
Ip	969.00		NIST
Ip	975.00		NIST
Ip	Outlier 1025.00		NIST
Ip	971.00		NIST
Ip	990.00		NIST
Ip	981.00		NIST
Ip	966.00		NIST
Ip	1005.00		NIST
Ip	982.00		NIST
Ip	969.00		NIST
Ip	979.00		NIST
Ip	980.00		NIST
Ip	944.00		NIST
Ip	983.00		NIST
Ip	Outlier 942.00		NIST
Ip	975.00		NIST
Ip	1009.00		NIST
Ip	996.00		NIST
Ip	970.00		NIST
Ip	969.00		NIST
Ip	966.00		NIST
Ip	986.00		NIST
Ip	992.00		NIST
Ip	975.00		NIST
Ip	983.00		NIST
Ip	984.00		NIST
Ip	998.00		NIST
Ip	974.00		NIST
Ip	980.00		NIST
Ip	984.00		NIST
Ip	970.00		NIST
Ip	965.00		NIST
Ip	1015.00		NIST
Ip	969.00		NIST
Ip	990.00		NIST
Ip	966.00		NIST
Ip	Outlier 1025.00		NIST
Ip	983.00		NIST
Ip	1005.00		NIST
Ip	943.00		NIST
Ip	975.00		NIST
Ip	977.00		NIST
Ip	983.40		NIST
S°liquid	[272.42; 274.10]	J/mol×K
S°liquid	274.10	J/mol×K	NIST
S°liquid	272.42	J/mol×K	NIST
Tboil	[362.05; 400.15]	K
Tboil	375.36	K	Measurement of Isobaric Vapor - Liquid Equilibria of Dimethyl Carbonate with Acetone, 2-Butanone and 2-Pentanone at 101.3 kPa and Density and Speed of Sound at 298.15 K
Tboil	375.39	K	ChemSep v8.3 pure component data Compiled value
Tboil	375.41	K	KDB
Tboil	375.15	K	NCMS SOLV-DB
Tboil	375.20	K	NIST
Tboil	375.40	K	NIST
Tboil	375.45 ± 0.30	K	NIST
Tboil	375.50 ± 0.30	K	NIST
Tboil	375.45	K	NIST
Tboil	375.41 ± 0.03	K	NIST
Tboil	375.05 ± 0.50	K	NIST
Tboil	375.00 ± 0.60	K	NIST
Tboil	375.00 ± 0.30	K	NIST
Tboil	375.10 ± 0.40	K	NIST
Tboil	375.10 ± 0.30	K	NIST
Tboil	375.95 ± 0.50	K	NIST
Tboil	375.15 ± 2.00	K	NIST
Tboil	375.45 ± 0.50	K	NIST
Tboil	375.15 ± 0.50	K	NIST
Tboil	375.55 ± 0.20	K	NIST
Tboil	373.65 ± 2.00	K	NIST
Tboil	375.42 ± 0.44	K	NIST
Tboil	375.95 ± 0.50	K	NIST
Tboil	375.25 ± 0.50	K	NIST
Tboil	375.35 ± 0.50	K	NIST
Tboil	375.50 ± 0.30	K	NIST
Tboil	375.45 ± 0.70	K	NIST
Tboil	373.90 ± 2.00	K	NIST
Tboil	375.15 ± 1.00	K	NIST
Tboil	375.50 ± 1.00	K	NIST
Tboil	375.15 ± 1.00	K	NIST
Tboil	374.65 ± 2.00	K	NIST
Tboil	375.15 ± 1.00	K	NIST
Tboil	375.40 ± 0.50	K	NIST
Tboil	373.15 ± 5.00	K	NIST
Tboil	376.15 ± 5.00	K	NIST
Tboil	375.08 ± 0.20	K	NIST
Tboil	375.15 ± 0.50	K	NIST
Tboil	374.15 ± 1.00	K	NIST
Tboil	373.15 ± 3.00	K	NIST
Tboil	376.15 ± 3.00	K	NIST
Tboil	375.65 ± 1.00	K	NIST
Tboil	375.30 ± 0.50	K	NIST
Tboil	374.65 ± 1.00	K	NIST
Tboil	375.25 ± 0.50	K	NIST
Tboil	375.55 ± 0.50	K	NIST
Tboil	375.15 ± 1.00	K	NIST
Tboil	375.40 ± 0.20	K	NIST
Tboil	374.15 ± 1.00	K	NIST
Tboil	375.15 ± 0.20	K	NIST
Tboil	375.45 ± 1.00	K	NIST
Tboil	375.15 ± 0.30	K	NIST
Tboil	375.65 ± 3.00	K	NIST
Tboil	376.15 ± 2.00	K	NIST
Tboil	374.95 ± 0.50	K	NIST
Tboil	375.15 ± 1.00	K	NIST
Tboil	Outlier 362.05 ± 1.00	K	NIST
Tboil	375.15 ± 1.00	K	NIST
Tboil	374.15 ± 2.00	K	NIST
Tboil	Outlier 400.15 ± 10.00	K	NIST
Tboil	374.15 ± 4.00	K	NIST
Tboil	374.15 ± 1.00	K	NIST
Tc	[561.08; 564.00]	K
Tc	561.10	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Tc	561.19	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	561.10	K	ChemSep v8.3 pure component data Compiled value
Tc	561.08	K	KDB
Tc	561.10	K	NIST
Tc	561.08 ± 0.20	K	NIST
Tc	Outlier 564.00 ± 0.56	K	NIST
Tfus	[194.00; 196.29]	K
Tfus	195.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	196.29	K	ChemSep v8.3 pure component data Compiled value
Tfus	196.20	K	KDB
Tfus	195.43	K	Aq. Solubility Prediction
Tfus	195.15	K	NCMS SOLV-DB
Tfus	195.65	K	NIST
Tfus	196.27 ± 0.02	K	NIST
Tfus	196.29 ± 0.01	K	NIST
Tfus	195.40 ± 0.25	K	NIST
Tfus	Outlier 194.00 ± 0.70	K	NIST
Tfus	195.40 ± 0.20	K	NIST
Ttriple	[196.29; 196.35]	K
Ttriple	196.29	K	ChemSep v8.3 pure component data Compiled value
Ttriple	196.31 ± 0.04	K	NIST
Ttriple	196.29 ± 0.07	K	NIST
Ttriple	196.35 ± 0.06	K	NIST
Ttriple	196.31 ± 0.04	K	NIST
Ttriple	196.29 ± 0.07	K	NIST
Ttriple	196.35 ± 0.06	K	NIST
UQi	3.42		ChemSep v8.3 pure component data Compiled value
URi	3.92		ChemSep v8.3 pure component data Compiled value
Vc	[0.301; 0.321]	m3/kmol
Vc	0.321	m3/kmol	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Vc	0.301	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.301	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.301	m3/kmol	KDB
Zc	[0.2380000; 0.2530000]
Zc	0.2530000		IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Zc	0.2380000		ChemSep v8.3 pure component data Compiled value
Zc	0.2383430		KDB
Zra	0.25		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[142.97; 167.15]	J/mol×K	[369.00; 454.00]
Cp,gas	142.97 ± 0.43	J/mol×K	369.00	NIST
Cp,gas	150.62 ± 0.45	J/mol×K	394.00	NIST
Cp,gas	156.40 ± 0.47	J/mol×K	414.00	NIST
Cp,gas	162.00 ± 0.49	J/mol×K	434.00	NIST
Cp,gas	167.15 ± 0.50	J/mol×K	454.00	NIST
Cp,liquid	[184.20; 185.40]	J/mol×K	[298.15; 298.15]
Cp,liquid	185.40	J/mol×K	298.15	NIST
Cp,liquid	185.10	J/mol×K	298.15	NIST
Cp,liquid	184.30	J/mol×K	298.15	NIST
Cp,liquid	184.20	J/mol×K	298.15	NIST
Cp,liquid	184.35	J/mol×K	298.15	NIST
η	[0.0004440; 0.0004960]	Pa×s	[293.15; 303.15]
η	0.0004960	Pa×s	293.15	Physical properties of the binary systems methylcyclopentane with ketones (acetone, butanone and 2-pentanone) at T = (293.15, 298.15, and 303.15) K. New UNIFAC-VISCO interaction parameters
η	0.0004960	Pa×s	293.15	Dynamic Viscosities of the Binary Systems Cyclohexane and Cyclopentane with Acetone, Butanone, or 2-Pentanone at Three Temperatures T ) (293.15, 298.15, and 303.15) K
η	0.0004690	Pa×s	298.15	Physical properties of the binary systems methylcyclopentane with ketones (acetone, butanone and 2-pentanone) at T = (293.15, 298.15, and 303.15) K. New UNIFAC-VISCO interaction parameters
η	0.0004690	Pa×s	298.15	Dynamic Viscosities of the Binary Systems Cyclohexane and Cyclopentane with Acetone, Butanone, or 2-Pentanone at Three Temperatures T ) (293.15, 298.15, and 303.15) K
η	0.0004890	Pa×s	298.15	NCMS SOLV-DB
η	0.0004440	Pa×s	303.15	Physical properties of the binary systems methylcyclopentane with ketones (acetone, butanone and 2-pentanone) at T = (293.15, 298.15, and 303.15) K. New UNIFAC-VISCO interaction parameters
η	0.0004440	Pa×s	303.15	Dynamic Viscosities of the Binary Systems Cyclohexane and Cyclopentane with Acetone, Butanone, or 2-Pentanone at Three Temperatures T ) (293.15, 298.15, and 303.15) K
ΔfusH	[2.09; 10.63]	kJ/mol	[110.00; 196.35]
ΔfusH	2.09	kJ/mol	110.00	NIST
ΔfusH	10.63	kJ/mol	196.30	NIST
ΔfusH	10.62	kJ/mol	196.35	NIST
ΔfusH	10.62	kJ/mol	196.35	NIST
ΔvapH	[32.20; 39.50]	kJ/mol	[320.50; 524.00]
ΔvapH	39.50	kJ/mol	320.50	NIST
ΔvapH	36.10 ± 0.10	kJ/mol	335.00	NIST
ΔvapH	36.50	kJ/mol	357.00	NIST
ΔvapH	34.40 ± 0.10	kJ/mol	360.00	NIST
ΔvapH	33.40 ± 0.10	kJ/mol	375.00	NIST
ΔvapH	33.47	kJ/mol	375.40	KDB
ΔvapH	33.44	kJ/mol	375.40	NIST
ΔvapH	36.10	kJ/mol	379.00	NIST
ΔvapH	32.80 ± 0.10	kJ/mol	386.00	NIST
ΔvapH	32.20 ± 0.10	kJ/mol	394.00	NIST
ΔvapH	33.70	kJ/mol	458.50	NIST
ΔvapH	33.30	kJ/mol	524.00	NIST
Pvap	4.72	kPa	298.15	NCMS SOLV-DB
n0	[1.38800; 1.39060]		[293.15; 298.15]
n0	1.39060		293.15	Isothermal Vapor-Liquid Equilibrium for the 2-Pentanone (MPK) + 2-Methyl Propan-1-ol Binary Mixture
n0	1.38930		293.15	Isothermal Vapor-Liquid Equilibrium Measurements for the Pentan-2-one + Propan-1-ol/Butan-1-ol System within 342-363 K
n0	1.38920		293.15	Solid-Liquid Equilibrium Measurements for Posaconazole and Voriconazole in Several Solvents between T = 278.2 and 323.2 K Using Differential Thermal Analysis/Thermal Gravimetric Analysis
n0	1.38930		293.15	Solubility Data for Roflumilast and Maraviroc in Various Solvents between T = (278.2-323.2) K
n0	1.38823		298.15	Properties of ionic liquid HMIMPF6 with carbonates, ketones and alkyl acetates
n0	1.38830		298.15	Excess molar volumes and ultrasonic studies of N-methyl-2-pyrrolidone with ketones at T = 303.15 K
n0	1.38810		298.15	Phase Equilibria in the Binary and Ternary Systems Composed of Diethyl ketone, 2-Pentanone and 3-Pentanol at 101.3 kPa
n0	1.38800		298.15	NCMS SOLV-DB
ρl	[762.27; 811.49]	kg/m3	[288.15; 338.15]
ρl	811.49	kg/m3	288.15	Excess molar volumes of (1-chlorobutane +heptane + 2-butanone or 2-pentanone) at 288.15 , 303.15 and 313.15 K . Measurements and correlations.
ρl	811.06	kg/m3	288.15	Thermal and Volumetric Properties of Some C5 and C6 Alkanones at Infinite Dilution in Water
ρl	806.00	kg/m3	293.00	KDB
ρl	807.47	kg/m3	293.15	Volumetric Properties of Binary Mixtures of N-Ethylformamide with Tetrahydropyran, 2-Pentanone, and Propylacetate from (293.15 to 313.15) K
ρl	806.83	kg/m3	293.15	Thermodynamics of amide + ketone mixtures. 1. Volumetric, speed of sound and refractive index data for N,N-dimethylformamide + 2-alkanone systems at several temperatures
ρl	801.52	kg/m3	298.15	Thermodynamics of Ketone + Amine Mixtures. Part VIII. Molar Excess Enthalpies at 298.15 K for n-Alkanone + Aniline or + N-Methylaniline Systems
ρl	801.52	kg/m3	298.15	Thermodynamics of ketone + amine mixtures. Part IX. Excess molar enthalpies at 298.15K for dipropylamine, or dibutylamine + 2-alkanone systems and modeling of linear or aromatic amine + 2-alkanone mixtures in terms of DISQUAC and ERAS
ρl	801.52	kg/m3	298.15	Thermodynamics of ketone + amine mixtures. Part X. Excess molarenthalpies at 298.15 K for N,N,N-triethylamine + 2-alkanone systems.Characterization of tertiary amine + 2-alkanone, and ofamino-ketone + n-alkane mixtures in terms of DISQUAC
ρl	802.46	kg/m3	298.15	Volumetric Properties of Binary Mixtures of N-Ethylformamide with Tetrahydropyran, 2-Pentanone, and Propylacetate from (293.15 to 313.15) K
ρl	801.99	kg/m3	298.15	Thermodynamics of amide + ketone mixtures. 1. Volumetric, speed of sound and refractive index data for N,N-dimethylformamide + 2-alkanone systems at several temperatures
ρl	801.41	kg/m3	298.15	Thermal and Volumetric Properties of Some C5 and C6 Alkanones at Infinite Dilution in Water
ρl	802.09	kg/m3	298.15	Density, Speed of Sound, and Refractive Index Measurements for Binary Mixtures of Pentan-2-one with Propan-2-ol and Butan-2-ol
ρl	797.53	kg/m3	303.15	Volumetric Properties of Binary Mixtures of N-Ethylformamide with Tetrahydropyran, 2-Pentanone, and Propylacetate from (293.15 to 313.15) K
ρl	796.73	kg/m3	303.15	Thermodynamics of amide + ketone mixtures. 1. Volumetric, speed of sound and refractive index data for N,N-dimethylformamide + 2-alkanone systems at several temperatures
ρl	796.58	kg/m3	303.15	Excess molar volumes and ultrasonic studies of dimethylsulphoxide with ketones at T = 303.15 K
ρl	796.96	kg/m3	303.15	Excess molar volumes of (1-chlorobutane +heptane + 2-butanone or 2-pentanone) at 288.15 , 303.15 and 313.15 K . Measurements and correlations.
ρl	791.66	kg/m3	308.15	Thermal and Volumetric Properties of Some C5 and C6 Alkanones at Infinite Dilution in Water
ρl	792.32	kg/m3	308.15	Density, Speed of Sound, and Refractive Index Measurements for Binary Mixtures of Pentan-2-one with Propan-2-ol and Butan-2-ol
ρl	792.52	kg/m3	308.15	Volumetric Properties of Binary Mixtures of N-Ethylformamide with Tetrahydropyran, 2-Pentanone, and Propylacetate from (293.15 to 313.15) K
ρl	787.16	kg/m3	313.15	Excess molar volumes of (1-chlorobutane +heptane + 2-butanone or 2-pentanone) at 288.15 , 303.15 and 313.15 K . Measurements and correlations.
ρl	787.44	kg/m3	313.15	Volumetric Properties of Binary Mixtures of N-Ethylformamide with Tetrahydropyran, 2-Pentanone, and Propylacetate from (293.15 to 313.15) K
ρl	782.44	kg/m3	318.15	Density, Speed of Sound, and Refractive Index Measurements for Binary Mixtures of Pentan-2-one with Propan-2-ol and Butan-2-ol
ρl	781.83	kg/m3	318.15	Thermal and Volumetric Properties of Some C5 and C6 Alkanones at Infinite Dilution in Water
ρl	772.43	kg/m3	328.15	Density, Speed of Sound, and Refractive Index Measurements for Binary Mixtures of Pentan-2-one with Propan-2-ol and Butan-2-ol
ρl	762.27	kg/m3	338.15	Density, Speed of Sound, and Refractive Index Measurements for Binary Mixtures of Pentan-2-one with Propan-2-ol and Butan-2-ol
ΔfusS	[2.18; 54.14]	J/mol×K	[110.00; 196.35]
ΔfusS	2.18	J/mol×K	110.00	NIST
ΔfusS	54.14	J/mol×K	196.30	NIST
ΔfusS	54.10	J/mol×K	196.35	NIST
ΔfusS	54.10	J/mol×K	196.35	NIST
csound,fluid	[1151.00; 1212.00]	m/s	[298.15; 313.15]
csound,fluid	1212.00	m/s	298.15	Vapor liquid equilibria for systems of diethyl carbonate and ketones and determination of group interaction parameters for the UNIFAC and ASOG methods
csound,fluid	1192.00	m/s	303.15	Densities and Speeds of Sound for Binary Liquid Mixtures of Thiolane-l,l-dioxide with Butanone, Pentan-2-one, Pentan-3-one, and 4-Methyl-pentan-2-one at T = (303.15 or 308.15 or 313.15) K
csound,fluid	1176.00	m/s	308.15	Densities and Speeds of Sound for Binary Liquid Mixtures of Thiolane-l,l-dioxide with Butanone, Pentan-2-one, Pentan-3-one, and 4-Methyl-pentan-2-one at T = (303.15 or 308.15 or 313.15) K
csound,fluid	1151.00	m/s	313.15	Densities and Speeds of Sound for Binary Liquid Mixtures of Thiolane-l,l-dioxide with Butanone, Pentan-2-one, Pentan-3-one, and 4-Methyl-pentan-2-one at T = (303.15 or 308.15 or 313.15) K
γ	0.03	N/m	298.15	NCMS SOLV-DB

Datasets

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
308.15	101.30	0.0004
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[97.92; 308.70]	J/mol×K	[200.00; 1500.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K
Coefficient A			8.69270e+01
Coefficient B			-7.27520e+02
Coefficient C			6.07824e+00
Coefficient D			-2.31610e-04
Coefficient E			6.92600e-08
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	97.92	J/mol×K	200.00	Calculated Property
Cp,gas	136.06	J/mol×K	344.44	Calculated Property
Cp,gas	176.36	J/mol×K	488.89	Calculated Property
Cp,gas	209.74	J/mol×K	633.33	Calculated Property
Cp,gas	236.03	J/mol×K	777.78	Calculated Property
Cp,gas	256.74	J/mol×K	922.22	Calculated Property
Cp,gas	273.34	J/mol×K	1066.67	Calculated Property
Cp,gas	286.99	J/mol×K	1211.11	Calculated Property
Cp,gas	298.56	J/mol×K	1355.56	Calculated Property
Cp,gas	308.70	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[172.53; 235.00]	J/mol×K	[196.29; 450.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K
Coefficient A			1.19520e+02
Coefficient B			1.55090e+02
Coefficient C			2.36804e+00
Coefficient D			3.83980e-03
Coefficient E			1.52360e-06
Temperature range, min.			196.29
Temperature range, max.			450.00
Cp,liquid	172.53	J/mol×K	196.29	Calculated Property
Cp,liquid	173.99	J/mol×K	224.48	Calculated Property
Cp,liquid	176.88	J/mol×K	252.67	Calculated Property
Cp,liquid	181.01	J/mol×K	280.86	Calculated Property
Cp,liquid	186.35	J/mol×K	309.05	Calculated Property
Cp,liquid	192.94	J/mol×K	337.24	Calculated Property
Cp,liquid	200.90	J/mol×K	365.43	Calculated Property
Cp,liquid	210.40	J/mol×K	393.62	Calculated Property
Cp,liquid	221.67	J/mol×K	421.81	Calculated Property
Cp,liquid	235.00	J/mol×K	450.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0009016; 0.0001439]	Pa×s	[250.00; 461.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-8.48120e+00
Coefficient B			9.21840e+02
Coefficient C			-4.09430e-01
Coefficient D			6.89840e-07
Coefficient E			2.00000e+00
Temperature range, min.			250.00
Temperature range, max.			461.00
η	0.0009016	Pa×s	250.00	Calculated Property
η	0.0006389	Pa×s	273.44	Calculated Property
η	0.0004777	Pa×s	296.89	Calculated Property
η	0.0003727	Pa×s	320.33	Calculated Property
η	0.0003007	Pa×s	343.78	Calculated Property
η	0.0002495	Pa×s	367.22	Calculated Property
η	0.0002118	Pa×s	390.67	Calculated Property
η	0.0001834	Pa×s	414.11	Calculated Property
η	0.0001613	Pa×s	437.56	Calculated Property
η	0.0001439	Pa×s	461.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[44.40; 0.79]	kJ/mol	[196.29; 561.08]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K
Coefficient A			6.07419e+01
Coefficient B			1.09782e+00
Coefficient C			-1.35015e+00
Coefficient D			9.26065e-01
Coefficient E			-2.50170e-01
Critical temperature, Tc (K)			5.61100e+02
Temperature range, min.			196.29
Temperature range, max.			561.08
ΔvapH	44.40	kJ/mol	196.29	Calculated Property
ΔvapH	41.97	kJ/mol	236.82	Calculated Property
ΔvapH	39.63	kJ/mol	277.35	Calculated Property
ΔvapH	37.26	kJ/mol	317.89	Calculated Property
ΔvapH	34.76	kJ/mol	358.42	Calculated Property
ΔvapH	32.01	kJ/mol	398.95	Calculated Property
ΔvapH	28.79	kJ/mol	439.48	Calculated Property
ΔvapH	24.76	kJ/mol	480.02	Calculated Property
ΔvapH	18.99	kJ/mol	520.55	Calculated Property
ΔvapH	0.79	kJ/mol	561.08	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.63]	kPa	[273.03; 399.81]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.49654e+01
Coefficient B			-3.57595e+03
Coefficient C			-2.93990e+01
Temperature range, min.			273.03
Temperature range, max.			399.81
Pvap	1.33	kPa	273.03	Calculated Property
Pvap	2.97	kPa	287.12	Calculated Property
Pvap	6.10	kPa	301.20	Calculated Property
Pvap	11.67	kPa	315.29	Calculated Property
Pvap	21.00	kPa	329.38	Calculated Property
Pvap	35.85	kPa	343.46	Calculated Property
Pvap	58.45	kPa	357.55	Calculated Property
Pvap	91.53	kPa	371.64	Calculated Property
Pvap	138.34	kPa	385.72	Calculated Property
Pvap	202.63	kPa	399.81	Calculated Property
Pvap	[7.38e-04; 3736.95]	kPa	[196.29; 561.10]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K
Coefficient A			8.51100e+01
Coefficient B			-7.34188e+03
Coefficient C			-1.04576e+01
Coefficient D			7.61086e-06
Coefficient E			2.00000e+00
Comment			Range stopped at Tc; ChemSep gives it to 561.15 K.
Temperature range, min.			196.29
Temperature range, max.			561.10
Pvap	7.38e-04	kPa	196.29	Calculated Property
Pvap	0.07	kPa	236.82	Calculated Property
Pvap	1.49	kPa	277.36	Calculated Property
Pvap	12.56	kPa	317.89	Calculated Property
Pvap	60.08	kPa	358.43	Calculated Property
Pvap	198.35	kPa	398.96	Calculated Property
Pvap	509.80	kPa	439.50	Calculated Property
Pvap	1102.94	kPa	480.03	Calculated Property
Pvap	2116.69	kPa	520.57	Calculated Property
Pvap	3736.95	kPa	561.10	Calculated Property
Pvap	[1.22; 257.19]	kPa	[275.00; 410.00]	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			1.05592e+02
Coefficient B			-8.16731e+03
Coefficient C			-1.36252e+01
Coefficient D			1.10014e-05
Coefficient E			0.00000e+00
Temperature range, min.			275.00
Temperature range, max.			410.00
Pvap	1.22	kPa	275.00	Calculated Property
Pvap	3.01	kPa	290.00	Calculated Property
Pvap	6.67	kPa	305.00	Calculated Property
Pvap	13.48	kPa	320.00	Calculated Property
Pvap	25.23	kPa	335.00	Calculated Property
Pvap	44.22	kPa	350.00	Calculated Property
Pvap	73.28	kPa	365.00	Calculated Property
Pvap	115.79	kPa	380.00	Calculated Property
Pvap	175.63	kPa	395.00	Calculated Property
Pvap	257.19	kPa	410.00	Calculated Property
Pvap	[20.43; 133.27]	kPa	[329.80; 384.80]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.41435e+01
Coefficient B			-3.01902e+03
Coefficient C			-5.84570e+01
Reference			Collerson, Counsell, et al., 1965, 2
Temperature range, min.			329.80
Temperature range, max.			384.80
Pvap	20.43	kPa	329.80	Calculated Property
Pvap	26.11	kPa	335.91	Calculated Property
Pvap	33.01	kPa	342.02	Calculated Property
Pvap	41.32	kPa	348.13	Calculated Property
Pvap	51.25	kPa	354.24	Calculated Property
Pvap	63.01	kPa	360.36	Calculated Property
Pvap	76.84	kPa	366.47	Calculated Property
Pvap	92.99	kPa	372.58	Calculated Property
Pvap	111.70	kPa	378.69	Calculated Property
Pvap	133.27	kPa	384.80	Calculated Property
Pvap	[24.93; 174.60]	kPa	[334.87; 394.57]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.41586e+01
Coefficient B			-3.01941e+03
Coefficient C			-5.89340e+01
Reference			Nickerson, Kobe, et al., 1961
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			334.87
Temperature range, max.			394.57
Pvap	24.93	kPa	334.87	Calculated Property
Pvap	32.23	kPa	341.50	Calculated Property
Pvap	41.19	kPa	348.14	Calculated Property
Pvap	52.05	kPa	354.77	Calculated Property
Pvap	65.11	kPa	361.40	Calculated Property
Pvap	80.66	kPa	368.04	Calculated Property
Pvap	99.04	kPa	374.67	Calculated Property
Pvap	120.57	kPa	381.30	Calculated Property
Pvap	145.63	kPa	387.94	Calculated Property
Pvap	174.60	kPa	394.57	Calculated Property
Pvap	[20.43; 133.27]	kPa	[329.80; 384.80]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.41435e+01
Coefficient B			-3.01902e+03
Coefficient C			-5.84570e+01
Reference			Collerson, Counsell, et al., 1965
Temperature range, min.			329.80
Temperature range, max.			384.80
Pvap	20.43	kPa	329.80	Calculated Property
Pvap	26.11	kPa	335.91	Calculated Property
Pvap	33.01	kPa	342.02	Calculated Property
Pvap	41.32	kPa	348.13	Calculated Property
Pvap	51.25	kPa	354.24	Calculated Property
Pvap	63.01	kPa	360.36	Calculated Property
Pvap	76.84	kPa	366.47	Calculated Property
Pvap	92.99	kPa	372.58	Calculated Property
Pvap	111.70	kPa	378.69	Calculated Property
Pvap	133.27	kPa	384.80	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[894.23; 291.45]	kg/m3	[196.29; 561.08]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K
Coefficient A			7.05682e+01
Coefficient B			2.59580e-01
Coefficient C			5.61100e+02
Coefficient D			2.89410e-01
Temperature range, min.			196.29
Temperature range, max.			561.08
ρl	894.23	kg/m3	196.29	Calculated Property
ρl	859.25	kg/m3	236.82	Calculated Property
ρl	822.58	kg/m3	277.35	Calculated Property
ρl	783.79	kg/m3	317.89	Calculated Property
ρl	742.27	kg/m3	358.42	Calculated Property
ρl	697.08	kg/m3	398.95	Calculated Property
ρl	646.58	kg/m3	439.48	Calculated Property
ρl	587.44	kg/m3	480.02	Calculated Property
ρl	510.70	kg/m3	520.55	Calculated Property
ρl	291.45	kg/m3	561.08	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 0.02]	N/m	[196.35; 375.15]	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			4.27813e-02
Coefficient B			-6.55000e-05
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			196.35
Temperature range, max.			375.15
γ	0.03	N/m	196.35	Calculated Property
γ	0.03	N/m	216.22	Calculated Property
γ	0.03	N/m	236.08	Calculated Property
γ	0.03	N/m	255.95	Calculated Property
γ	0.02	N/m	275.82	Calculated Property
γ	0.02	N/m	295.68	Calculated Property
γ	0.02	N/m	315.55	Calculated Property
γ	0.02	N/m	335.42	Calculated Property
γ	0.02	N/m	355.28	Calculated Property
γ	0.02	N/m	375.15	Calculated Property
γ	[0.03; 7.37e-06]	N/m	[196.29; 559.62]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K
Coefficient A			-3.95600e-02
Coefficient B			2.19190e+00
Coefficient C			-2.40930e+00
Coefficient D			-8.79100e-04
Coefficient E			-1.06140e-06
Comment			Range stopped where the equation turns negative; ChemSep gives it to 561.08 K.
Temperature range, min.			196.29
Temperature range, max.			559.62
γ	0.03	N/m	196.29	Calculated Property
γ	0.03	N/m	236.66	Calculated Property
γ	0.03	N/m	277.03	Calculated Property
γ	0.02	N/m	317.40	Calculated Property
γ	0.02	N/m	357.77	Calculated Property
γ	0.01	N/m	398.14	Calculated Property
γ	0.01	N/m	438.51	Calculated Property
γ	0.01	N/m	478.88	Calculated Property
γ	0.00	N/m	519.25	Calculated Property
γ	7.37e-06	N/m	559.62	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.00; 0.12]	W/m×K	[196.29; 1000.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K
Coefficient A			-1.79120e-02
Coefficient B			4.82500e-01
Coefficient C			-3.88770e+03
Coefficient D			-1.29630e+06
Temperature range, min.			196.29
Temperature range, max.			1000.00
λgas	0.00	W/m×K	196.29	Calculated Property
λgas	0.01	W/m×K	285.59	Calculated Property
λgas	0.02	W/m×K	374.89	Calculated Property
λgas	0.03	W/m×K	464.19	Calculated Property
λgas	0.04	W/m×K	553.49	Calculated Property
λgas	0.05	W/m×K	642.80	Calculated Property
λgas	0.06	W/m×K	732.10	Calculated Property
λgas	0.08	W/m×K	821.40	Calculated Property
λgas	0.10	W/m×K	910.70	Calculated Property
λgas	0.12	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.17; 0.09]	W/m×K	[196.29; 513.15]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is λliquid in W/m×K, T in K
Coefficient A			1.08890e-02
Coefficient B			-3.66580e+01
Coefficient C			-1.22060e+00
Coefficient D			-2.24130e-03
Coefficient E			-2.52110e-07
Temperature range, min.			196.29
Temperature range, max.			513.15
λliquid	0.17	W/m×K	196.29	Calculated Property
λliquid	0.16	W/m×K	231.50	Calculated Property
λliquid	0.15	W/m×K	266.70	Calculated Property
λliquid	0.14	W/m×K	301.91	Calculated Property
λliquid	0.13	W/m×K	337.12	Calculated Property
λliquid	0.12	W/m×K	372.32	Calculated Property
λliquid	0.11	W/m×K	407.53	Calculated Property
λliquid	0.11	W/m×K	442.74	Calculated Property
λliquid	0.10	W/m×K	477.94	Calculated Property
λliquid	0.09	W/m×K	513.15	Calculated Property

Similar Compounds

Find more compounds similar to 2-Pentanone.

Mixtures

• 2-Pentanone + Triethylamine
• Cyclopentane, methyl- + 2-Pentanone
• 2-Pentanone + Formamide, N,N-dimethyl-
• 2-Pentanone + Dimethyl Sulfoxide
• 2-Pentanone + 2-Pyrrolidinone, 1-methyl-
• 2-Pentanone + Water
• 2-Pentanone + sodium sulphate + Water
• Phenol, 2-methyl- + 2-Pentanone + Water
• Phenol, 3-methyl- + 2-Pentanone + Water
• PHENOL, 4-METHYL- + 2-Pentanone + Water
• Diethyl carbonate + 2-Pentanone
• 2-Pentanone + 1-Propanamine, N-propyl-
• 2-Pentanone + 1-Butanamine, N-butyl-
• 2-Pentanone + Butane, 1-chloro-
• 2-Pentanone + Heptane
• 2-Pentanone + Butane, 1-chloro- + Heptane
• 2-Pentanone + Tetrahydropyran
• 2-Pentanone + Carbonic acid, dimethyl ester
• 2-Pentanone + Cyclohexane
• 2-Pentanone + Cyclopentane

Find more mixtures with 2-Pentanone.

Sources

• KDB Vapor Pressure Data
• 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 7 ChEDL chemicals 1.5.2, from Kudchadker, A. P.; Ambrose, D.; Tsonopoulos, C. Vapor-Liquid Critical Properties of Elements and Compounds. 7. Oxygen Compounds Other Than Alkanols and Cycloalkanols. J. Chem. Eng. Data 2001, 46, 457-479.
• 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.
• 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.
• A relative headspace method for Henry s constants of volatile organic compounds
• Vapor liquid equilibria for systems of diethyl carbonate and ketones and determination of group interaction parameters for the UNIFAC and ASOG methods
• Liquid liquid equilibria of 1,3-dimethylimidazolium methyl sulfate with ketones, dialkyl carbonates and acetates
• Thermodynamics of ketone + amine mixtures. Part IX. Excess molar enthalpies at 298.15K for dipropylamine, or dibutylamine + 2-alkanone systems and modeling of linear or aromatic amine + 2-alkanone mixtures in terms of DISQUAC and ERAS
• Thermodynamics of ketone + amine mixtures. Part X. Excess molarenthalpies at 298.15 K for N,N,N-triethylamine + 2-alkanone systems.Characterization of tertiary amine + 2-alkanone, and ofamino-ketone + n-alkane mixtures in terms of DISQUAC
• 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
• Activity coefficients at infinite dilution for different alcohols and ketones in [EMpy][ESO4]: Experimental data and modeling with PC-SAFT
• Activity coefficients at infinite dilution of organic solvents and water in 1-butyl-3-methylimidazolium dicyanamide. A literature review of hexane/hex-1-ene separation
• High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
• Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
• Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-butyl-1-methylpyrrolidinium dicyanamide
• New ionic liquid [P4,4,4,4][NTf2] in bio-butanol extraction on investigation of limiting activity coefficients
• Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
• A thermodynamic study of the ketoreductase-catalyzed reduction of 2-alkanones in non-aqueous solvents
• Thermodynamics of binary mixtures of N-methyl-2-pyrrolidinone and ketone. Experimental results and modelling of the solid-liquid equilibrium and vapou-liquid equilibrium. The Modified UNIFAC (Do) model characterization
• Systems with ionic liquids: Measurement of VLE and c1 data and prediction of their thermodynamic behavior using original UNIFAC, mod. UNIFAC(Do) and COSMO-RS(Ol)
• Properties of ionic liquid HMIMPF6 with carbonates, ketones and alkyl acetates
• (Liquid + liquid) phase equilibria of 1-alkyl-3-methylimidazolium methylsulfate with alcohols, or ethers, or ketones
• Physical properties of the binary systems methylcyclopentane with ketones (acetone, butanone and 2-pentanone) at T = (293.15, 298.15, and 303.15) K. New UNIFAC-VISCO interaction parameters
• Measurement of activity coefficients at infinite dilution in 1-hexadecyl-3-methylimidazolium tetrafluoroborate ionic liquid
• Excess molar volumes and ultrasonic studies of dimethylsulphoxide with ketones at T = 303.15 K
• Excess molar volumes and ultrasonic studies of N-methyl-2-pyrrolidone with ketones at T = 303.15 K
• Measurements of activity coefficients at infinite dilution of organic solutes and water in 1-propyl-1-methylpiperidinium bis{(trifluoromethyl)sulfonyl}imide ionic liquid using g.l.c.
• Measurements of activity coefficients at infinite dilution of organic compounds and water in isoquinolinium-based ionic liquid [C8iQuin][NTf2] using GLC
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(3-hydroxypropyl)pyridinium bis(trifluoromethylsulfonyl)-amide
• Thermodynamics and activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tetracyanoborate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-hexyl-3-methylimidazolium tetracyanoborate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpiperidinium bis(trifluoromethylsulfonyl)-amide
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpyrrolidinium bis(trifluoromethylsulfonyl)-amide
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium trifluorotris(perfluoroethyl)phosphate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpiperidinium trifluorotris(perfluoroethyl)phosphate
• Physicochemical properties and activity coefficients at infinite dilution for organic solutes and water in a novel bicyclic guanidinium superbase-derived protic ionic liquid
• Experimental and theoretical study on infinite dilution activity coefficients of various solutes in piperidinium ionic liquids
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpyrrolidinium trifluorotris(perfluoroethyl)phosphate
• Measurements of activity coefficients at infinite dilution for organic solutes and water in N-hexylisoquinolinium thiocyanate, [HiQuin][SCN] using GLC
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-hydroxyethyl)- 3-methylimidazolium trifluorotris(perfluoroethyl)phosphate
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tricyanomethanide
• Thermodynamics and activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylmorpholinium tricyanomethanide
• The study of activity coefficients at infinite dilution for organic solutes and water in 1-butyl-4-methylpyridinium dicyanamide, [B4MPy][DCA] using GLC
• Measurement of activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-hexyl-1,4-diaza[2.2.2]bicyclooctanium bis(trifluoromethylsulfonyl)imide using gas-liquid chromatography
• Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
• Solvation parameter model and thermodynamic parameters in a dicationic ionic liquid based on pyrrolidinium
• Experimental and theoretically study of interaction between organic compounds and tricyanomethanide based ionic liquids
• Activity coefficients at infinite dilution of organic solutes in methylphosphonate based ionic liquids using gas-liquid chromatography
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(3-hydroxypropyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
• Activity coefficients at infinite dilution for organic solutes and water in 1-ethyl-1-methylpyrrolidinium lactate
• Activity coefficients at infinite dilution, physicochemical and thermodynamic properties for organic solutes and water in the ionic liquid ethyl-dimethyl-(2-methoxyethyl)ammonium trifluorotris-(perfluoroethyl)phosphate
• Screening of environmental friendly ionic liquid as a solvent for the different types of separations problem: Insight from activity coefficients at infinite dilution measurement using (gas + liquid) chromatography technique
• A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
• Thermodynamics of amide + ketone mixtures. 1. Volumetric, speed of sound and refractive index data for N,N-dimethylformamide + 2-alkanone systems at several temperatures
• Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in 1-allyl-3-methylimidazolium bis{(trifluoromethyl)sulfonyl}imide ionic liquid
• Separation of aliphatic from aromatic hydrocarbons and sulphur compounds from fuel based on measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid N,N-diethyl-N-methyl-N-(2-methoxy-ethyl)ammonium bis(trifluoromethylsulfonyl)imide
• Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
• Measurement and thermodynamic modeling of ternary (liquid + liquid) equilibrium for extraction of o-cresol, m-cresol or p-cresol from aqueous solution with 2-pentanone
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
• Separation of water/butan-1-ol based on activity coefficients at infinite dilution in 1,3-didecyl-2-methylimidazolium dicyanamide ionic liquid
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on gamma infinity data measurements
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid trihexyl-tetradecyl-phosphonium tricyanomethanide
• Thermodynamic study of molecular interaction-selectivity in separation processes based on limiting activity coefficients
• The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
• Improving the method of solution calorimetry for evaluation of the enthalpies of phase transitions and condensed state enthalpies of formation
• Excess molar volumes of (1-chlorobutane +heptane + 2-butanone or 2-pentanone) at 288.15 , 303.15 and 313.15 K . Measurements and correlations.
• 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
• Thermodynamic of dissolution and hydrogen bond of the pyrrole, N-methylpyrrole with proton acceptors
• Enthalpies of solution and enthalpies of solvation of organic solutes in ethylene glycol at 298.15 K: Prediction and analysis of intermolecular interaction contributions
• Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
• Thermal and Volumetric Properties of Some C5 and C6 Alkanones at Infinite Dilution in Water
• Liquid-Liquid Equilibria for Ternary (Methyl Propyl Ketone + Hydroquinone or Resorcinol + Water) Systems at 298.15, 318.15, and 333.15 K
• Solubility Measurement and Thermodynamic Modeling of Benzoic Acid in Monosolvents and Binary Mixtures
• Liquid-Liquid Equilibrium for Ternary Systems of 2-Pentanone/Mesityl Oxide + Catechol + Water at 298.2, 318.2, and 333.2 K
• Isothermal Vapor-Liquid Equilibrium for the 2-Pentanone (MPK) + 2-Methyl Propan-1-ol Binary Mixture
• Density, Speed of Sound, and Refractive Index Measurements for Binary Mixtures of Pentan-2-one with Propan-2-ol and Butan-2-ol
• Thermodynamic Parameters of a New Synthesized Tricationic Ionic Liquid Stationary Phase by Inverse Gas Chromatography
• Isothermal Vapor-Liquid Equilibrium Measurements for the Pentan-2-one + Propan-1-ol/Butan-1-ol System within 342-363 K
• Solid-Liquid Equilibrium Measurements for Posaconazole and Voriconazole in Several Solvents between T = 278.2 and 323.2 K Using Differential Thermal Analysis/Thermal Gravimetric Analysis
• Measurements and Thermodynamic Modeling of Liquid-Liquid Equilibria Data for the Ternary (Methyl Propyl Ketone + Catechol/Resorcinol/Hydroquinone + Water) Systems
• Solubility Data for Roflumilast and Maraviroc in Various Solvents between T = (278.2-323.2) K
• Air-Water Partitioning of C5 and C6 Alkanones: Measurement, Critical Compilation, Correlation, and Recommended Data
• Thermodynamics of mixtures involving some linear or cyclic ketones and cyclic ethers. 2. Systems containing tetrahydropyran
• Phase Equilibria in the Binary and Ternary Systems Composed of Diethyl ketone, 2-Pentanone and 3-Pentanol at 101.3 kPa
• Thermodynamics of Mixtures Involving Some Linear or Cyclic Ketones and Cyclic Ethers. 3. Systems Containing 1,4-Dioxane
• Thermodynamics of Mixtures Involving Some Linear or Cyclic Ketones and Cyclic Ethers. 4. Systems Containing 1,3-Dioxolane
• Determination of Henry s Law Constants and Activity Coefficients at Infinite Dilution of Flavor Compounds in Water at 298 K with a Gas-Chromatographic Method
• Measurement of Isobaric Vapor - Liquid Equilibria of Dimethyl Carbonate with Acetone, 2-Butanone and 2-Pentanone at 101.3 kPa and Density and Speed of Sound at 298.15 K
• Measurement of Activity Coefficients at Infinite Dilution of Benzene, Toluene, Ethanol, Esters, Ketones, and Ethers at Various Temperatures in Water Using the Dilutor Technique
• Dynamic Viscosities of the Binary Systems Cyclohexane and Cyclopentane with Acetone, Butanone, or 2-Pentanone at Three Temperatures T ) (293.15, 298.15, and 303.15) K
• 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
• Henry s Constants of 1-Alkanols and 2-Ketones in Salt Solutions
• Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Butyl-3-methyl-pyridinium Trifluoromethanesulfonate
• Determination of Activity Coefficients at Infinite Dilution of 35 Solutes in the Ionic Liquid, 1-Butyl-3-methylimidazolium Tosylate, Using Gas-Liquid Chromatography
• Measurements of Activity Coefficients at Infinite Dilution for Organic Solutes and Water in the Ionic Liquid 1-Butyl-1-methylpiperydinium Thiocyanate
• Activity Coefficients at Infinite Dilution of Organic Compounds in Four New Imidazolium-Based Ionic Liquids
• Thermodynamics of Ketone + Amine Mixtures. Part VIII. Molar Excess Enthalpies at 298.15 K for n-Alkanone + Aniline or + N-Methylaniline Systems
• Partition Coefficients of Organic Compounds in Four New Tetraalkylammonium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Using Inverse Gas Chromatography
• Evaluation of the Performance of Trigeminal Tricationic Ionic Liquids for Separation Problems
• 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
• Volumetric Properties of Binary Mixtures of N-Ethylformamide with Tetrahydropyran, 2-Pentanone, and Propylacetate from (293.15 to 313.15) K
• Activity Coefficients at Infinite Dilution for Organic Solutes Dissolved in Three 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Bearing Short Linear Alkyl Side Chains of Three to Five Carbons
• Infinite Dilution Activity Coefficients of Solutes Dissolved in Two Trihexyl(tetradecyl)phosphonium Ionic Liquids
• Phase Equilibria of (1-Ethyl-3-methylimidazolium Ethylsulfate + Hydrocarbon, + Ketone, and + Ether) Binary Systems
• Volumetric and Transport Properties of Binary Liquid Mixtures of Aliphatic Ketones with Phenylacetonitrile at T = 308.15 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
• Densities and Speeds of Sound for Binary Liquid Mixtures of Thiolane-l,l-dioxide with Butanone, Pentan-2-one, Pentan-3-one, and 4-Methyl-pentan-2-one at T = (303.15 or 308.15 or 313.15) K
• Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
• 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

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