Chemical Properties of Thiophene (CAS 110-02-1)

InChI

InChI=1S/C4H4S/c1-2-4-5-3-1/h1-4H

InChI Key

YTPLMLYBLZKORZ-UHFFFAOYSA-N

Formula

C4H4S

SMILES

c1ccsc1

Molecular Weight¹

84.14

CAS

110-02-1

Other Names

• CP 34
• Divinylene sulfide
• Furan, thio-
• Hopkin's lactic acid reagent
• Huile H50
• Huile HSO
• NSC 405073
• Thiacyclopentadiene
• Thiaphene
• Thiofen
• Thiofuram
• Thiofuran
• Thiofurfuran
• Thiole
• Thiophen
• Thiotetrole
• UN 2414
• USAF EK-1860

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• BasG : Gas basicity (kJ/mol).
• μ : Dipole Moment (debye).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_subH : Enthalpy of sublimation at a given temperature (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• V_c : Critical Volume (m³/kmol).
• Z_c : Critical Compressibility.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Contents

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

Physical Properties

Property	Value	Unit	Source
ω	0.1960		KDB
PAff	815.00	kJ/mol	NIST
BasG	784.30	kJ/mol	NIST
μ	0.50	debye	KDB
ΔfG°	126.90	kJ/mol	KDB
ΔfH°gas	[115.00; 218.40]	kJ/mol
ΔfH°gas	115.80	kJ/mol	KDB
ΔfH°gas	218.40	kJ/mol	NIST
ΔfH°gas	116.40	kJ/mol	NIST
ΔfH°gas	115.00 ± 1.00	kJ/mol	NIST
ΔfH°gas	116.70	kJ/mol	NIST
ΔvapH°	[34.60; 35.40]	kJ/mol
ΔvapH°	34.79	kJ/mol	NIST
ΔvapH°	34.60	kJ/mol	NIST
ΔvapH°	34.70 ± 0.03	kJ/mol	NIST
ΔvapH°	35.40	kJ/mol	NIST
IE	[8.80; 9.12]	eV
IE	8.86 ± 0.02	eV	NIST
IE	8.85	eV	NIST
IE	8.85	eV	NIST
IE	9.00 ± 0.10	eV	NIST
IE	8.87 ± 0.01	eV	NIST
IE	8.80	eV	NIST
IE	8.80 ± 0.05	eV	NIST
IE	8.90	eV	NIST
IE	Outlier 9.05	eV	NIST
IE	8.87 ± 0.01	eV	NIST
IE	Outlier 9.12 ± 0.05	eV	NIST
IE	8.87 ± 0.01	eV	NIST
IE	8.86 ± 0.01	eV	NIST
IE	8.80 ± 0.05	eV	NIST
IE	8.87 ± 0.05	eV	NIST
IE	8.86 ± 0.01	eV	NIST
IE	8.95 ± 0.02	eV	NIST
IE	8.85	eV	NIST
IE	8.90	eV	NIST
IE	8.90	eV	NIST
IE	8.85	eV	NIST
IE	8.87	eV	NIST
log10WS	[-1.45; -1.33]
log10WS	-1.45		Aq. Solubility Prediction
log10WS	-1.33		Estimated Solubility
logPoct/wat	1.748		Crippen Calculated Property
McVol	64.110	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
NFPA Health	2		KDB
Pc	[5690.00; 5700.00]	kPa
Pc	5690.00	kPa	KDB
Pc	5700.00 ± 68.94	kPa	NIST
Inp	[626.00; 703.00]
Inp	694.00		NIST
Inp	686.10		NIST
Inp	700.00		NIST
Inp	674.60		NIST
Inp	679.60		NIST
Inp	685.30		NIST
Inp	668.00		NIST
Inp	668.00		NIST
Inp	668.00		NIST
Inp	683.00		NIST
Inp	686.00		NIST
Inp	694.00		NIST
Inp	675.00		NIST
Inp	694.00		NIST
Inp	664.60		NIST
Inp	641.00		NIST
Inp	648.00		NIST
Inp	693.00		NIST
Inp	644.00		NIST
Inp	632.00		NIST
Inp	644.00		NIST
Inp	632.00		NIST
Inp	693.00		NIST
Inp	670.00		NIST
Inp	671.00		NIST
Inp	652.00		NIST
Inp	690.00		NIST
Inp	672.00		NIST
Inp	703.00		NIST
Inp	673.00		NIST
Inp	665.00		NIST
Inp	665.00		NIST
Inp	649.00		NIST
Inp	671.00		NIST
Inp	658.00		NIST
Inp	668.00		NIST
Inp	648.00		NIST
Inp	650.00		NIST
Inp	646.00		NIST
Inp	648.00		NIST
Inp	661.00		NIST
Inp	661.00		NIST
Inp	Outlier 626.00		NIST
Inp	636.00		NIST
Inp	686.00		NIST
Inp	675.00		NIST
Inp	680.00		NIST
Inp	693.00		NIST
Inp	655.00		NIST
Inp	648.00		NIST
Inp	646.00		NIST
Inp	647.00		NIST
Inp	643.23		NIST
Inp	685.00		NIST
Inp	650.00		NIST
Inp	677.00		NIST
Inp	644.00		NIST
Inp	645.00		NIST
Inp	644.00		NIST
Inp	645.00		NIST
Inp	665.00		NIST
Inp	650.00		NIST
Inp	665.00		NIST
Inp	667.00		NIST
Inp	647.00		NIST
Inp	694.00		NIST
Inp	680.00		NIST
Inp	651.00		NIST
Inp	653.00		NIST
Inp	665.00		NIST
Inp	650.00		NIST
Inp	647.00		NIST
Inp	700.00		NIST
Inp	686.00		NIST
Inp	694.00		NIST
Inp	685.30		NIST
Inp	641.00		NIST
Inp	644.00		NIST
Inp	652.00		NIST
Inp	672.00		NIST
Inp	649.00		NIST
Inp	650.00		NIST
I	[995.00; 1054.00]
I	Outlier 1054.00		NIST
I	1039.00		NIST
I	1046.00		NIST
I	1023.00		NIST
I	1017.00		NIST
I	1023.00		NIST
I	1028.00		NIST
I	1022.00		NIST
I	1028.00		NIST
I	1034.00		NIST
I	1030.00		NIST
I	1010.00		NIST
I	1024.00		NIST
I	1024.00		NIST
I	1026.00		NIST
I	1021.00		NIST
I	1021.00		NIST
I	1021.00		NIST
I	1041.00		NIST
I	Outlier 995.00		NIST
I	1022.00		NIST
I	1035.00		NIST
I	1032.00		NIST
I	1034.00		NIST
I	1032.00		NIST
I	1035.00		NIST
I	1035.00		NIST
I	Outlier 1054.00		NIST
I	1022.00		NIST
I	1025.00		NIST
I	1018.00		NIST
I	1017.00		NIST
I	1010.00		NIST
I	1021.00		NIST
I	1035.00		NIST
I	Outlier 1054.00		NIST
Tboil	[356.80; 357.90]	K
Tboil	357.42	K	Isobaric vapor-liquid equilibrium for four binary systems of thiophene
Tboil	357.42	K	Isobaric vapor-liquid equilibrium for systems containing sulfur compounds
Tboil	357.10	K	KDB
Tboil	357.40	K	NIST
Tboil	357.26 ± 0.20	K	NIST
Tboil	357.30	K	NIST
Tboil	357.35 ± 0.10	K	NIST
Tboil	356.80 ± 0.50	K	NIST
Tboil	Outlier 357.90 ± 0.50	K	NIST
Tboil	357.15 ± 0.50	K	NIST
Tc	[579.40; 580.00]	K
Tc	579.40	K	KDB
Tc	579.40	K	NIST
Tc	579.40 ± 0.30	K	NIST
Tc	580.00 ± 2.00	K	NIST
Tfus	[233.15; 234.94]	K
Tfus	233.70	K	KDB
Tfus	234.68	K	Aq. Solubility Prediction
Tfus	234.93 ± 0.05	K	NIST
Tfus	234.94 ± 0.10	K	NIST
Tfus	233.15 ± 0.40	K	NIST
Ttriple	[233.70; 235.02]	K
Ttriple	235.02 ± 0.05	K	NIST
Ttriple	234.90 ± 0.08	K	NIST
Ttriple	234.95 ± 0.06	K	NIST
Ttriple	233.70 ± 0.40	K	NIST
Vc	[0.219; 0.220]	m3/kmol
Vc	0.219	m3/kmol	KDB
Vc	0.220 ± 0.005	m3/kmol	NIST
Zc	0.2586670		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
ΔfusH	4.97	kJ/mol	235.20	NIST
ΔsubH	[46.80; 49.00]	kJ/mol	[202.50; 211.50]
ΔsubH	49.00	kJ/mol	202.50	NIST
ΔsubH	46.80	kJ/mol	211.50	NIST
ΔvapH	[31.46; 35.80]	kJ/mol	[258.50; 357.30]
ΔvapH	35.00	kJ/mol	258.50	NIST
ΔvapH	33.60 ± 0.10	kJ/mol	319.00	NIST
ΔvapH	35.80	kJ/mol	324.00	NIST
ΔvapH	34.10	kJ/mol	333.00	NIST
ΔvapH	32.70 ± 0.10	kJ/mol	336.00	NIST
ΔvapH	33.70	kJ/mol	352.00	NIST
ΔvapH	34.80	kJ/mol	353.00	NIST
ΔvapH	32.60	kJ/mol	353.50	NIST
ΔvapH	31.46	kJ/mol	357.00	KDB
ΔvapH	31.50 ± 0.10	kJ/mol	357.00	NIST
ΔvapH	31.48	kJ/mol	357.30	NIST
Pvap	[2.78; 119.90]	kPa	[273.15; 363.15]
Pvap	2.78	kPa	273.15	Measurement and correlation of vapour pressures of pyridine and thiophene with [EMIM][SCN] ionic liquid
Pvap	4.89	kPa	283.15	Measurement and correlation of vapour pressures of pyridine and thiophene with [EMIM][SCN] ionic liquid
Pvap	6.78	kPa	288.15	Experimental Measurement and Modeling of Phase Diagrams of Binary Systems Encountered in the Gasoline Desulfurization Process Using Ionic Liquids
Pvap	6.75	kPa	288.15	Experimental Measurement and Modeling of Phase Diagrams of Binary Systems Encountered in the Gasoline Desulfurization Process Using Ionic Liquids
Pvap	8.74	kPa	293.15	Experimental Measurement and Modeling of Phase Diagrams of Binary Systems Encountered in the Gasoline Desulfurization Process Using Ionic Liquids
Pvap	8.22	kPa	293.15	Measurement and correlation of vapour pressures of pyridine and thiophene with [EMIM][SCN] ionic liquid
Pvap	8.70	kPa	293.15	Experimental Measurement and Modeling of Phase Diagrams of Binary Systems Encountered in the Gasoline Desulfurization Process Using Ionic Liquids
Pvap	10.37	kPa	298.15	Experimental Measurement and Modeling of Phase Diagrams of Binary Systems Encountered in the Gasoline Desulfurization Process Using Ionic Liquids
Pvap	10.58	kPa	298.15	Experimental Measurement and Modeling of Phase Diagrams of Binary Systems Encountered in the Gasoline Desulfurization Process Using Ionic Liquids
Pvap	12.98	kPa	303.15	Experimental Measurement and Modeling of Phase Diagrams of Binary Systems Encountered in the Gasoline Desulfurization Process Using Ionic Liquids
Pvap	13.29	kPa	303.15	Vapor Pressure Measurements for Binary Mixtures Containing Ionic Liquid and Predictions by the Conductor-like Screening Model for Real Solvents
Pvap	13.23	kPa	303.15	Measurement and correlation of vapour pressures of pyridine and thiophene with [EMIM][SCN] ionic liquid
Pvap	16.70	kPa	308.12	Vapor-Liquid Equilibrium for Thiophene + Butane, + trans-But-2-ene, + 2-Methylpropane, and + 2-Methylpropene
Pvap	16.50	kPa	308.13	Vapor-Liquid Equilibrium for Thiophene + Butane, + trans-But-2-ene, + 2-Methylpropane, and + 2-Methylpropene
Pvap	17.10	kPa	308.14	Vapor-Liquid Equilibrium for Thiophene + Butane, + trans-But-2-ene, + 2-Methylpropane, and + 2-Methylpropene
Pvap	16.61	kPa	308.15	Vapor Pressure Measurements for Binary Mixtures Containing Ionic Liquid and Predictions by the Conductor-like Screening Model for Real Solvents
Pvap	17.10	kPa	308.15	Vapor-Liquid Equilibrium for Thiophene + Butane, + trans-But-2-ene, + 2-Methylpropane, and + 2-Methylpropene
Pvap	20.59	kPa	313.15	Vapor Pressure Measurements for Binary Mixtures Containing Ionic Liquid and Predictions by the Conductor-like Screening Model for Real Solvents
Pvap	20.52	kPa	313.15	Measurement and correlation of vapour pressures of pyridine and thiophene with [EMIM][SCN] ionic liquid
Pvap	25.31	kPa	318.15	Vapor Pressure Measurements for Binary Mixtures Containing Ionic Liquid and Predictions by the Conductor-like Screening Model for Real Solvents
Pvap	30.87	kPa	323.15	Vapor Pressure Measurements for Binary Mixtures Containing Ionic Liquid and Predictions by the Conductor-like Screening Model for Real Solvents
Pvap	30.80	kPa	323.15	Measurement and correlation of vapour pressures of pyridine and thiophene with [EMIM][SCN] ionic liquid
Pvap	37.40	kPa	328.15	Vapor Pressure Measurements for Binary Mixtures Containing Ionic Liquid and Predictions by the Conductor-like Screening Model for Real Solvents
Pvap	44.98	kPa	333.15	Vapor Pressure Measurements for Binary Mixtures Containing Ionic Liquid and Predictions by the Conductor-like Screening Model for Real Solvents
Pvap	44.88	kPa	333.15	Measurement and correlation of vapour pressures of pyridine and thiophene with [EMIM][SCN] ionic liquid
Pvap	49.70	kPa	335.61	Vapor-Liquid Equilibrium for Thiophene + Butane, + trans-But-2-ene, + 2-Methylpropane, and + 2-Methylpropene
Pvap	49.60	kPa	335.84	Vapor-Liquid Equilibrium for Thiophene + Butane, + trans-But-2-ene, + 2-Methylpropane, and + 2-Methylpropene
Pvap	49.60	kPa	335.87	Vapor-Liquid Equilibrium for Thiophene + Butane, + trans-But-2-ene, + 2-Methylpropane, and + 2-Methylpropene
Pvap	51.20	kPa	336.83	Vapor-Liquid Equilibrium for Thiophene + Butane, + trans-But-2-ene, + 2-Methylpropane, and + 2-Methylpropene
Pvap	63.71	kPa	343.15	Measurement and correlation of vapour pressures of pyridine and thiophene with [EMIM][SCN] ionic liquid
Pvap	88.33	kPa	353.15	Measurement and correlation of vapour pressures of pyridine and thiophene with [EMIM][SCN] ionic liquid
Pvap	119.90	kPa	363.15	Measurement and correlation of vapour pressures of pyridine and thiophene with [EMIM][SCN] ionic liquid
n0	[1.52530; 1.52869]		[298.10; 298.15]
n0	1.52530		298.10	Liquid-Liquid Equilibria for [C8mim][NTf2] + Thiophene + 2,2,4-Trimethylpentane or + Toluene
n0	1.52550		298.15	Vapor liquid equilibrium for binary system of thiophene + 2,2,4-trimethylpentane at 343.15 and 353.15K and thiophene + 2-ethoxy-2-methylpropane at 333.15 and 343.15K
n0	1.52581		298.15	Phase behaviour of 1-methyl-3-octylimidazolium bis[trifluoromethylsulfonyl]imide with thiophene and aliphatic hydrocarbons: The influence of n-alkane chain length
n0	1.52530		298.15	Thiophene separation from aliphatic hydrocarbons using the 1-ethyl-3-methylimidazolium ethylsulfate ionic liquid
n0	1.52581		298.15	(Liquid + liquid) equilibria of [C8mim][NTf2] ionic liquid with a sulfur-component and hydrocarbons
n0	1.52550		298.15	Vapor-Liquid Equilibrium for Binary System of 1-Propanethiol, Thiophene, and Diethyl Sulfide with Toluene at 90.03 kPa
n0	1.52550		298.15	Vapor-Liquid Equilibrium for Binary System of Thiophene + n-Hexane at (338.15 and 323.15) K and Thiophene + 1-Hexene at (333.15 and 323.15) K
n0	1.52869		298.15	Vapor Liquid Equilibrium for Methoxymethane + Thiophene, + Diethylsulfide, + 2-Methyl-2-propanethiol and 1-Hexene, + 1-Propanethiol
n0	1.52581		298.15	Liquid-Liquid Equilibria for Systems Composed by 1-Methyl-3-octylimidazolium Tetrafluoroborate Ionic Liquid, Thiophene, and n-Hexane or Cyclohexane
n0	1.52581		298.15	Measurement and Correlation of Liquid-Liquid Equilibria of Two Imidazolium Ionic Liquids with Thiophene and Methylcyclohexane
ρl	[1058.46; 1071.00]	kg/m3	[289.00; 298.15]
ρl	1071.00	kg/m3	289.00	KDB
ρl	1058.64	kg/m3	298.15	Separation of sulfur compounds from alkanes with 1-alkylcyanopyridinium-based ionic liquids
ρl	1058.61	kg/m3	298.15	Desulfurization of fuels by liquid-liquid extraction with1-ethyl-3-methylimidazolium ionic liquids
ρl	1058.48	kg/m3	298.15	Phase behaviour of tricyanomethanide-based ionic liquids with alcohols and hydrocarbons
ρl	1058.56	kg/m3	298.15	Phase diagrams of binary systems containing tricyanomethanide-based ionic liquids and thiophene or pyridine - new experimental data and PC-SAFT modeling
ρl	1058.50	kg/m3	298.15	Solvent extraction of thiophene from n-alkanes (C7, C12, and C16) using the ionic liquid [C8mim][BF4]
ρl	1058.61	kg/m3	298.15	Hexyl dimethylpyridinium ionic liquids for desulfurization of fuels. Effect of the position of the alkyl side chains
ρl	1058.92	kg/m3	298.15	Effect of the alkyl side chain of the 1-alkylpiperidinium-based ionic liquids on desulfurization of fuels
ρl	1058.92	kg/m3	298.15	Extraction desulfurization process of fuels with ionic liquids
ρl	1058.56	kg/m3	298.15	Volumetric, acoustic, and refractometric properties of (thiophene + hexane/cyclohexane) solutions in the presence of some imidazolium based ionic liquids at T = 298.15 K
ρl	1058.46	kg/m3	298.15	Measurements and equation-of-state modelling of thermodynamic properties of binary mixtures of 1-butyl-1-methylpyrrolidinium tetracyanoborate ionic liquid with molecular compounds
ρl	1058.56	kg/m3	298.15	Thermodynamic behavior of thiophene with octane, 1-hexyl-3-methylimidazolium bromide, or 1-octyl-3-methylimidazolium bromide in dilute region at T = (288.15 to 303.15) K
ρl	1058.48	kg/m3	298.15	Phase behaviour of ionic liquid 1-butyl-1-methylpyrrolidinium tris(pentafluoroethyl)trifluorophosphate with alcohols, water and aromatic hydrocarbons
γ	0.03	N/m	293.20	KDB

Datasets

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.15	101.00	1063.59
303.15	101.00	1051.55
313.09	1029.00	1040.96
313.09	1969.00	1041.84
313.09	2970.00	1042.78
313.09	3987.00	1043.71
313.09	5055.00	1044.72
313.09	5952.00	1045.51
313.09	6937.00	1046.43
313.09	8032.00	1047.39
313.09	9218.00	1048.44
313.09	10045.00	1049.18
313.09	11012.00	1050.03
313.09	12014.00	1050.9
313.09	12995.00	1051.74
313.09	13961.00	1052.59
313.09	14970.00	1053.43
313.09	15953.00	1054.26
313.09	17004.00	1055.16
313.09	18003.00	1055.95
313.09	18904.00	1056.76
313.15	101.00	1039.32
323.01	1047.00	1028.97
323.01	2059.00	1029.98
323.01	3070.00	1031.02
323.01	4047.00	1031.99
323.01	5002.00	1032.9
323.01	6005.00	1033.9
323.01	7068.00	1034.92
323.01	8021.00	1035.81
323.01	9013.00	1036.76
323.01	10005.00	1037.67
323.01	10991.00	1038.62
323.01	12034.00	1039.58
323.01	12977.00	1040.44
323.01	13999.00	1041.38
323.01	14991.00	1042.26
323.01	15995.00	1043.17
323.01	16998.00	1044.03
323.01	17983.00	1044.93
323.01	18951.00	1045.78
323.15	101.00	1026.98
332.85	1015.00	1016.93
332.85	2035.00	1018.0
332.85	3004.00	1019.06
332.85	3964.00	1020.05
332.85	4991.00	1021.14
332.85	6001.00	1022.17
332.85	7014.00	1023.21
332.85	7998.00	1024.2
332.85	9009.00	1025.23
332.85	9995.00	1026.19
332.85	10989.00	1027.18
332.85	12006.00	1028.17
332.85	13009.00	1029.18
332.85	13971.00	1030.09
332.85	15006.00	1031.04
332.85	15990.00	1032.01
332.85	17050.00	1033.03
332.85	17976.00	1033.88
332.85	19018.00	1034.92
333.15	101.00	1014.58
342.77	1039.00	1004.75
342.77	2072.00	1005.93
342.77	3033.00	1007.02
342.77	4023.00	1008.17
342.77	5027.00	1009.26
342.77	6033.00	1010.36
342.77	7008.00	1011.44
342.77	7998.00	1012.5
342.77	9005.00	1013.59
342.77	10000.00	1014.65
342.77	10963.00	1015.65
342.77	12009.00	1016.72
342.77	13023.00	1017.82
342.77	13928.00	1018.74
342.77	15009.00	1019.83
342.77	15998.00	1020.79
342.77	17025.00	1021.8
342.77	17995.00	1022.8
342.77	19013.00	1023.79
342.77	20001.00	1024.73
343.15	101.00	1002.15
352.67	1064.00	992.39
352.67	2003.00	993.54
352.67	3024.00	994.79
352.67	4003.00	995.98
352.67	5048.00	997.22
352.67	6013.00	998.36
352.67	7013.00	999.51
352.67	8050.00	1000.73
352.67	9018.00	1001.82
352.67	10003.00	1002.93
352.67	11003.00	1004.07
352.67	12004.00	1005.16
352.67	12998.00	1006.25
352.67	14005.00	1007.34
352.67	15038.00	1008.46
352.67	16006.00	1009.49
352.67	17027.00	1010.58
352.67	18001.00	1011.6
352.67	19031.00	1012.65
352.67	20017.00	1013.74
353.15	101.00	989.76
362.51	1007.00	979.8
362.51	2022.00	981.13
362.51	3029.00	982.49
362.51	4004.00	983.74
362.51	5006.00	985.01
362.51	6003.00	986.27
362.51	6999.00	987.5
362.51	7993.00	988.73
362.51	9007.00	989.99
362.51	9993.00	991.16
362.51	10997.00	992.36
362.51	11993.00	993.56
362.51	12838.00	994.53
362.51	14038.00	995.94
362.51	15044.00	997.1
362.51	16029.00	998.18
362.51	17006.00	999.27
362.51	18016.00	1000.4
362.51	18987.00	1001.47
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	1058.44
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.15	100.00	1076.4
288.15	100.00	1070.54
293.15	100.00	1064.59
298.15	100.00	1058.65
303.15	100.00	1052.71
308.15	100.00	1046.7
313.15	100.00	1040.68
318.15	100.00	1034.64
323.15	100.00	1028.59
328.15	100.00	1022.43
333.15	100.00	1016.27
338.15	100.00	1010.08
283.15	2000.00	1077.94
288.15	2000.00	1072.11
293.15	2000.00	1066.21
298.15	2000.00	1060.32
303.15	2000.00	1054.43
308.15	2000.00	1048.48
313.15	2000.00	1042.52
318.15	2000.00	1036.54
323.15	2000.00	1030.52
328.15	2000.00	1024.49
333.15	2000.00	1018.35
338.15	2000.00	1012.22
283.15	5000.00	1080.27
288.15	5000.00	1074.53
293.15	5000.00	1068.67
298.15	5000.00	1062.91
303.15	5000.00	1057.07
308.15	5000.00	1051.21
313.15	5000.00	1045.35
318.15	5000.00	1039.44
323.15	5000.00	1033.54
328.15	5000.00	1027.57
333.15	5000.00	1021.56
338.15	5000.00	1015.53
283.15	7000.00	1081.81
288.15	7000.00	1076.12
293.15	7000.00	1070.33
298.15	7000.00	1064.57
303.15	7000.00	1058.82
308.15	7000.00	1052.99
313.15	7000.00	1047.19
318.15	7000.00	1041.36
323.15	7000.00	1035.52
328.15	7000.00	1029.6
333.15	7000.00	1023.65
338.15	7000.00	1017.69
283.15	10000.00	1084.09
288.15	10000.00	1078.46
293.15	10000.00	1072.75
298.15	10000.00	1067.05
303.15	10000.00	1061.36
308.15	10000.00	1055.61
313.15	10000.00	1049.91
318.15	10000.00	1044.15
323.15	10000.00	1038.37
328.15	10000.00	1032.58
333.15	10000.00	1026.72
338.15	10000.00	1020.86
283.15	15000.00	1087.78
288.15	15000.00	1082.24
293.15	15000.00	1076.63
298.15	15000.00	1071.07
303.15	15000.00	1065.48
308.15	15000.00	1059.87
313.15	15000.00	1054.25
318.15	15000.00	1048.65
323.15	15000.00	1042.99
328.15	15000.00	1037.33
333.15	15000.00	1031.63
338.15	15000.00	1025.92
283.15	20000.00	1091.37
288.15	20000.00	1085.9
293.15	20000.00	1080.39
298.15	20000.00	1074.94
303.15	20000.00	1069.46
308.15	20000.00	1063.97
313.15	20000.00	1058.47
318.15	20000.00	1052.97
323.15	20000.00	1047.45
328.15	20000.00	1041.91
333.15	20000.00	1036.34
338.15	20000.00	1030.78
283.15	25000.00	1094.82
288.15	25000.00	1089.45
293.15	25000.00	1084.05
298.15	25000.00	1078.69
303.15	25000.00	1073.3
308.15	25000.00	1067.92
313.15	25000.00	1062.52
318.15	25000.00	1057.12
323.15	25000.00	1051.73
328.15	25000.00	1046.31
333.15	25000.00	1040.87
338.15	25000.00	1035.41
283.15	30000.00	1098.18
288.15	30000.00	1092.91
293.15	30000.00	1087.58
298.15	30000.00	1082.3
303.15	30000.00	1077.03
308.15	30000.00	1071.73
313.15	30000.00	1066.43
318.15	30000.00	1061.15
323.15	30000.00	1055.85
328.15	30000.00	1050.54
333.15	30000.00	1045.21
338.15	30000.00	1039.88
283.15	35000.00	1101.44
288.15	35000.00	1096.24
293.15	35000.00	1091.01
298.15	35000.00	1085.81
303.15	35000.00	1080.62
308.15	35000.00	1075.4
313.15	35000.00	1070.21
318.15	35000.00	1065.02
323.15	35000.00	1059.82
328.15	35000.00	1054.61
333.15	35000.00	1049.39
338.15	35000.00	1044.17
283.15	40000.00	1104.61
288.15	40000.00	1099.5
293.15	40000.00	1094.34
298.15	40000.00	1089.21
303.15	40000.00	1084.1
308.15	40000.00	1078.99
313.15	40000.00	1073.88
318.15	40000.00	1068.77
323.15	40000.00	1063.67
328.15	40000.00	1058.55
333.15	40000.00	1053.43
338.15	40000.00	1048.31
283.15	45000.00	1107.7
288.15	45000.00	1102.65
293.15	45000.00	1097.57
298.15	45000.00	1092.53
303.15	45000.00	1087.49
308.15	45000.00	1082.45
313.15	45000.00	1077.41
318.15	45000.00	1072.41
323.15	45000.00	1067.38
328.15	45000.00	1062.36
333.15	45000.00	1057.32
338.15	45000.00	1052.28
283.15	50000.00	1110.71
288.15	50000.00	1105.72
293.15	50000.00	1100.7
298.15	50000.00	1095.73
303.15	50000.00	1090.79
308.15	50000.00	1085.8
313.15	50000.00	1080.86
318.15	50000.00	1075.92
323.15	50000.00	1070.98
328.15	50000.00	1066.05
333.15	50000.00	1061.09
338.15	50000.00	1056.13
283.15	55000.00	1113.62
288.15	55000.00	1108.7
293.15	55000.00	1103.77
298.15	55000.00	1098.86
303.15	55000.00	1093.96
308.15	55000.00	1089.07
313.15	55000.00	1084.2
318.15	55000.00	1079.33
323.15	55000.00	1074.48
328.15	55000.00	1069.6
333.15	55000.00	1064.72
338.15	55000.00	1059.87
283.15	60000.00	1116.47
288.15	60000.00	1111.61
293.15	60000.00	1106.72
298.15	60000.00	1101.89
303.15	60000.00	1097.06
308.15	60000.00	1092.23
313.15	60000.00	1087.42
318.15	60000.00	1082.65
323.15	60000.00	1077.86
328.15	60000.00	1073.07
333.15	60000.00	1068.26
338.15	60000.00	1063.48
283.15	65000.00	1119.27
288.15	65000.00	1114.44
293.15	65000.00	1109.63
298.15	65000.00	1104.85
303.15	65000.00	1100.09
308.15	65000.00	1095.31
313.15	65000.00	1090.59
318.15	65000.00	1085.87
323.15	65000.00	1081.13
328.15	65000.00	1076.42
333.15	65000.00	1071.7
338.15	65000.00	1066.99
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[0.19; 5693.44]	kPa	[234.94; 579.35]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.42640e+01
Coefficient B			-2.98618e+03
Coefficient C			-4.77130e+01
Temperature range, min.			234.94
Temperature range, max.			579.35
Pvap	0.19	kPa	234.94	Calculated Property
Pvap	2.78	kPa	273.21	Calculated Property
Pvap	18.96	kPa	311.48	Calculated Property
Pvap	79.60	kPa	349.74	Calculated Property
Pvap	241.98	kPa	388.01	Calculated Property
Pvap	587.51	kPa	426.28	Calculated Property
Pvap	1212.04	kPa	464.55	Calculated Property
Pvap	2213.77	kPa	502.81	Calculated Property
Pvap	3682.68	kPa	541.08	Calculated Property
Pvap	5693.44	kPa	579.35	Calculated Property
Pvap	[0.19; 5690.84]	kPa	[234.94; 579.35]	KDB Vapor Pressure Data
Equation			ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K
Coefficient A			8.19473e+01
Coefficient B			-6.84652e+03
Coefficient C			-1.00558e+01
Coefficient D			7.42178e-06
Coefficient E			0.00000e+00
Temperature range, min.			234.94
Temperature range, max.			579.35
Pvap	0.19	kPa	234.94	Calculated Property
Pvap	2.79	kPa	273.21	Calculated Property
Pvap	19.16	kPa	311.48	Calculated Property
Pvap	79.87	kPa	349.74	Calculated Property
Pvap	238.99	kPa	388.01	Calculated Property
Pvap	570.14	kPa	426.28	Calculated Property
Pvap	1161.50	kPa	464.55	Calculated Property
Pvap	2117.24	kPa	502.81	Calculated Property
Pvap	3568.04	kPa	541.08	Calculated Property
Pvap	5690.84	kPa	579.35	Calculated Property
Pvap	[44.85; 172.80]	kPa	[333.40; 373.50]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.62727e+01
Coefficient B			-4.12236e+03
Coefficient C			-2.80500e+00
Reference			Eon, Pommier, et al., 1971
Temperature range, min.			333.40
Temperature range, max.			373.50
Pvap	44.85	kPa	333.40	Calculated Property
Pvap	52.93	kPa	337.86	Calculated Property
Pvap	62.21	kPa	342.31	Calculated Property
Pvap	72.81	kPa	346.77	Calculated Property
Pvap	84.86	kPa	351.22	Calculated Property
Pvap	98.54	kPa	355.68	Calculated Property
Pvap	113.99	kPa	360.13	Calculated Property
Pvap	131.39	kPa	364.59	Calculated Property
Pvap	150.93	kPa	369.04	Calculated Property
Pvap	172.80	kPa	373.50	Calculated Property
Pvap	[19.91; 270.13]	kPa	[312.21; 392.94]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.39849e+01
Coefficient B			-2.85423e+03
Coefficient C			-5.25850e+01
Reference			Waddington, Knowlton, et al., 1949, 2
Temperature range, min.			312.21
Temperature range, max.			392.94
Pvap	19.91	kPa	312.21	Calculated Property
Pvap	28.74	kPa	321.18	Calculated Property
Pvap	40.52	kPa	330.15	Calculated Property
Pvap	55.91	kPa	339.12	Calculated Property
Pvap	75.65	kPa	348.09	Calculated Property
Pvap	100.55	kPa	357.06	Calculated Property
Pvap	131.49	kPa	366.03	Calculated Property
Pvap	169.40	kPa	375.00	Calculated Property
Pvap	215.27	kPa	383.97	Calculated Property
Pvap	270.13	kPa	392.94	Calculated Property
Pvap	[19.91; 270.13]	kPa	[312.21; 392.94]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.39849e+01
Coefficient B			-2.85423e+03
Coefficient C			-5.25850e+01
Reference			Waddington, Knowlton, et al., 1949
Temperature range, min.			312.21
Temperature range, max.			392.94
Pvap	19.91	kPa	312.21	Calculated Property
Pvap	28.74	kPa	321.18	Calculated Property
Pvap	40.52	kPa	330.15	Calculated Property
Pvap	55.91	kPa	339.12	Calculated Property
Pvap	75.65	kPa	348.09	Calculated Property
Pvap	100.55	kPa	357.06	Calculated Property
Pvap	131.49	kPa	366.03	Calculated Property
Pvap	169.40	kPa	375.00	Calculated Property
Pvap	215.27	kPa	383.97	Calculated Property
Pvap	270.13	kPa	392.94	Calculated Property

Similar Compounds

Find more compounds similar to Thiophene.

Mixtures

• Thiophene + Water
• Thiophene + Heptane + Ethanol, 2,2'-oxybis-
• Thiophene + Triethylene glycol + Heptane
• 1,2-Ethanediol + Thiophene + TETRAMETHYLAMMONIUM CHLORIDE
• Carbon dioxide + Thiophene
• Thiophene + 2-Butene, 2,3-dimethyl-
• Thiophene + Heptane
• 1-Propanol + Carbon dioxide + Thiophene
• Thiophene + Pentane, 2,2,4-trimethyl-
• Thiophene + Propane, 2-ethoxy-2-methyl-
• Benzene + Thiophene
• Benzene + 2-Pyrrolidinone, 1-methyl- + Thiophene
• Carbon dioxide + Thiophene + Nonane
• Carbon dioxide + Thiophene + Decane
• Thiophene + TETRAMETHYLAMMONIUM CHLORIDE + Glycerin
• 1,2-Ethanediol + Thiophene
• Thiophene + Ethanol, 2,2'-oxybis-
• Thiophene + Triethylene glycol
• Monoethanolamine + Thiophene
• ETHANOL, 2,2'-IMINOBIS- + Thiophene

Find more mixtures with Thiophene.

Sources

• KDB Vapor Pressure Data
• Crippen Method
• Solubility of thiopene in carbon dioxide and carbon dioxide + 1-propanol mixtures at temperatures from 313 to 363K
• High pressure vapor liquid equilibria for the systems thiophene + nonane +CO2, and thiophene + decane +CO2
• Compressed liquid densities and excess volumes of CO2 + thiophene binary mixtures from 313 to 363 K and pressures up to 25 MPa
• Infinite dilution activity coefficient measurements by inert gas stripping method
• Vapor liquid equilibrium for binary system of thiophene + 2,2,4-trimethylpentane at 343.15 and 353.15K and thiophene + 2-ethoxy-2-methylpropane at 333.15 and 343.15K
• Phase behaviour of 1-methyl-3-octylimidazolium bis[trifluoromethylsulfonyl]imide with thiophene and aliphatic hydrocarbons: The influence of n-alkane chain length
• Thiophene separation from aliphatic hydrocarbons using the 1-ethyl-3-methylimidazolium ethylsulfate ionic liquid
• Measurement and correlation of vapor pressure of benzene and thiophene with BMIM][PF6] and [BMIM][BF4] ionic liquids
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium trifluoromethanesulfonate using GLC
• Activity coefficients at infinite dilution measurements for organic solutes and water in the 1-hexyloxymethyl-3-methyl-imidazolium and 1,3-dihexyloxymethyl-imidazolium bis(trifluoromethylsulfonyl)-imide ionic liquids The cation influence
• Ionic liquids on desulfurization of fuel oils
• Liquid-liquid equilibrium and interfacial tension of the ternary system heptane + thiophene + 1-ethyl-3-methylimidazolium bis(trifluoromethanesulfonyl)imide
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
• Influence of the ionic liquid structure on thiophene solubility
• Hexyl dimethylpyridinium ionic liquids for desulfurization of fuels. Effect of the position of the alkyl side chains
• Isobaric vapor-liquid equilibrium for four binary systems of thiophene
• Ternary liquid-liquid equilibria of bis(trifluoromethylsulfonyl)-amide based ionic liquids + thiophene + n-heptane. The influence of cation structure
• Phase behaviour of ionic liquid 1-butyl-1-methylpyrrolidinium tris(pentafluoroethyl)trifluorophosphate with alcohols, water and aromatic hydrocarbons
• Isobaric vapor-liquid equilibrium for systems containing sulfur compounds
• Desulfurization of fuels by liquid-liquid extraction with1-ethyl-3-methylimidazolium ionic liquids
• 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
• Phase behaviour of tricyanomethanide-based ionic liquids with alcohols and hydrocarbons
• Separation of benzene and thiophene with a mixture of N-methyl-2- pyrrolidinone (NMP) and ionic liquid as the entrainer
• Phase diagrams of binary systems containing tricyanomethanide-based ionic liquids and thiophene or pyridine - new experimental data and PC-SAFT modeling
• Novel liquid-liquid equilibrium data for six ternary systems containing IL, hydrocarbon and thiophene at 25 C
• Liquid-liquid equilibria in the ternary and multicomponent systems involving hydrocarbons, thiophene or pyridine and ionic liquid (1-benzyl-3-metylimidazolium bis(trifluorometylsulfonyl)imide)
• 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
• Effect of cation alkyl chain length on liquid-liquid equilibria of {ionic liquids + thiophene + heptane}: COSMO-RS prediction and experimental verification
• High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
• Liquid-liquid equilibrium data for extractive desulfurization using 1-butyl-3-methyl imidazolium thiocyanate, n-alkane and thiophene
• Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
• Measurements of activity coefficient at infinite dilution for organic solutes in tetramethylammonium chloride + ethylene glycol deep eutectic solvent using gas-liquid chromatography
• Tetramethylammonium chloride + glycerol deep eutectic solvent as separation agent for organic liquid mixtures: Assessment from experimental limiting activity coefficients
• Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-butyl-1-methylpyrrolidinium dicyanamide
• Extraction of benzothiazole and thiophene from their mixtures with n-heptane using tetrahexylammonium bromide-based deep eutectic solvents as extractive denitrogenation and desulfurization agents
• 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
• Separation of thiophene, or benzothiophene from model fuel using glycols. Liquid-liquid phase equilibria and oxidative desulfurization study
• Effective extraction of benzene and thiophene by novel deep eutectic solvents from hexane / aromatic mixture at different temperatures
• Application of trihexyltetradecylphosphonium dicyanamide ionic liquid for various types of separations problems: Activity coefficients at infinite dilution measurements utilizing GLC method
• Measurement of activity coefficients at infinite dilution in 1-hexadecyl-3-methylimidazolium tetrafluoroborate ionic liquid
• (Liquid + liquid) equilibria of [C8mim][NTf2] ionic liquid with a sulfur-component and hydrocarbons
• Solvent extraction of thiophene from n-alkanes (C7, C12, and C16) using the ionic liquid [C8mim][BF4]
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid triethylsulphonium bis(trifluoromethylsulfonyl)imide
• Measurements of activity coefficients at infinite dilution of aliphatic and aromatic hydrocarbons, alcohols, thiophene, tetrahydrofuran, MTBE, and water in ionic liquid [BMIM][SCN] using GLC
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 4-methyl-N-butyl-pyridinium bis(trifluoromethylsulfonyl)-imide
• Gas liquid chromatography measurements of activity coefficients at infinite dilution of various organic solutes and water in tri-iso-butylmethylphosphonium tosylate ionic liquid
• Evaluation of the polysubstituted pyridinium ionic liquid [hmmpy][Ntf2] as a suitable solvent for desulfurization: Phase equilibria
• 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
• Interactions of volatile organic compounds with 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 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
• Ternary (liquid + liquid) equilibria of {trifluorotris(perfluoroethyl)phosphate based ionic liquids + thiophene + heptane}
• 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
• Desulfurization of fuel-oils with [C2mim][NTf2]: A comparative study
• Interactions of volatile organic compounds with the ionic liquids 1-butyl-1-methylpyrrolidinium tetracyanoborate and 1-butyl-1-methylpyrrolidinium bis(oxalato)borate
• 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
• Separation of thiophene from heptane with ionic liquids
• Measurements of activity coefficients at infinite dilution for organic solutes and water in N-hexylisoquinolinium thiocyanate, [HiQuin][SCN] using GLC
• Quaternary (liquid +liquid) equilibria for systems of imidazolium based ionic liquid + thiophene + pyridine + cyclohexane at 298.15 K: Experiments and quantum chemical predictions
• Phase equilibria study of the (N-octylisoquinolinium thiocyanate ionic liquid + aliphatic and aromatic hydrocarbon, or thiophene) binary systems
• 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
• Infinite dilution activity coefficients of volatile organic compounds in two ionic liquids composed of the tris(pentafluoroethyl) trifluorophosphate ([FAP]) anion and a functionalized cation
• Solvent extraction of aromatic sulfur compounds from n-heptane using the 1-ethyl-3-methylimidazolium tricyanomethanide ionic liquid
• 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
• Separation of sulfur compounds from alkanes with 1-alkylcyanopyridinium-based ionic liquids
• Effect of the alkyl side chain of the 1-alkylpiperidinium-based ionic liquids on desulfurization of fuels
• Measurement and correlation of vapour pressures of pyridine and thiophene with [EMIM][SCN] ionic liquid
• Application of 1-pentyl-3-methylimidazolium bis(trifluoromethylsulfonyl) imide for desulfurization, denitrification and dearomatization of FCC gasoline
• Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
• Extraction desulfurization process of fuels with ionic liquids
• Ternary (liquid + liquid) equilibria of {trifluorotris(perfluoroethyl) phosphate based ionic liquids + thiophene + heptane}: Part 2
• Phase equilibria study of binary systems comprising an (ionic liquid + hydrocarbon)
• 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
• Volumetric, acoustic, and refractometric properties of (thiophene + hexane/cyclohexane) solutions in the presence of some imidazolium based ionic liquids at T = 298.15 K
• 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
• Measurements and equation-of-state modelling of thermodynamic properties of binary mixtures of 1-butyl-1-methylpyrrolidinium tetracyanoborate ionic liquid with molecular compounds
• Thermodynamic behavior of thiophene with octane, 1-hexyl-3-methylimidazolium bromide, or 1-octyl-3-methylimidazolium bromide in dilute region at T = (288.15 to 303.15) K
• A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
• 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
• Densities at high pressures and derived properties of thiophenes
• Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
• 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
• Liquid-liquid extraction of sulfur compounds from heptane with tricyanomethanide based ionic liquids
• Ternary liquid-liquid phase equilibria of {ionic liquid + thiophene + (octane/hexadecane)}
• Separation of (water/butan-1-ol) binary systems based on activity coefficients at infinite dilution with phosphonium ionic liquid
• Additive scheme for calculation of solvation enthalpies of heterocyclic aromatic compounds. Sublimation/vaporization enthalpy at 298.15 K
• Vapor Pressure Measurements for Binary Mixtures Containing Ionic Liquid and Predictions by the Conductor-like Screening Model for Real Solvents
• Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
• Liquid Liquid Equilibria for the Ternary Systems Dodecane + Toluene or Thiophene or Pyridine + 1-Ethyl-3-methylimidazolium Methyl Sulfate
• Elimination of Tar in Biomass Gasification Process: Liquid Liquid Equilibrium of Ternary Systems {Water + Solvent (p-Xylene and Methyl Hexadecanoate) + Model Molecules of Tar (Thiophene, Pyridine, Naphthalene, Phenathrene, and Anthracene)}
• Effect of the Type of Ammonium Salt on the Extractive Desulfurization of Fuels Using Deep Eutectic Solvents
• Activity Coefficients at Infinite Dilution of Various Solutes in Tetrapropylammonium Bromide + 1,6-Hexanediol Deep Eutectic Solvent
• Experimental Measurements and Modeling Study of Liquid-Liquid Equilibrium [(Water + Methyl Oleate + Model Molecules of Tar Issued from the Biomass Gasification Process (Benzene, Toluene, Phenol, Thiophene, and Pyridine)]
• Assessment of Pyrrolidinium-Based Ionic Liquid for the Separation of Binary Mixtures Based on Activity Coefficients at Infinite Dilution
• Experimental Determination of the Solubility of Thiophene in Carbon Dioxide and in Carbon Dioxide + Ethanol
• 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
• Vapor-Liquid Equilibrium for Binary System of 1-Propanethiol, Thiophene, and Diethyl Sulfide with Toluene at 90.03 kPa
• Vapor-Liquid Equilibrium for Binary System of Thiophene + n-Hexane at (338.15 and 323.15) K and Thiophene + 1-Hexene at (333.15 and 323.15) K
• 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
• Vapor-Liquid Equilibrium for Thiophene + Butane, + trans-But-2-ene, + 2-Methylpropane, and + 2-Methylpropene
• Activity Coefficients at Infinite Dilution of Organic Compounds in Four New Imidazolium-Based Ionic Liquids
• 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
• 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
• Vapor Liquid Equilibrium for Methoxymethane + Thiophene, + Diethylsulfide, + 2-Methyl-2-propanethiol and 1-Hexene, + 1-Propanethiol
• 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
• Experimental Measurement and Modeling of Phase Diagrams of Binary Systems Encountered in the Gasoline Desulfurization Process Using Ionic Liquids
• Infinite Dilution Activity Coefficients of Solutes Dissolved in Two Trihexyl(tetradecyl)phosphonium Ionic Liquids
• Liquid-Liquid Equilibria for Systems Composed by 1-Methyl-3-octylimidazolium Tetrafluoroborate Ionic Liquid, Thiophene, and n-Hexane or Cyclohexane
• Solubilities of the Gaseous and Liquid Solutes and Their Thermodynamics of Solubilization in the Novel Room-Temperature Ionic Liquids at Infinite Dilution by Gas Chromatography
• Measurement and Correlation of Liquid-Liquid Equilibria of Two Imidazolium Ionic Liquids with Thiophene and Methylcyclohexane
• Liquid-Liquid Equilibria for [C8mim][NTf2] + Thiophene + 2,2,4-Trimethylpentane or + Toluene
• Liquid-Liquid Equilibria of Ternary Systems Sulfide + Octane + Solvents at Different 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
• 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
• Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Hexyl-3-methylimidazolium Thiocyanate
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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