Chemical Properties of Pentane, 2,2,4-trimethyl- (CAS 540-84-1)

InChI

InChI=1S/C8H18/c1-7(2)6-8(3,4)5/h7H,6H2,1-5H3

InChI Key

NHTMVDHEPJAVLT-UHFFFAOYSA-N

Formula

C8H18

SMILES

CC(C)CC(C)(C)C

Molecular Weight¹

114.23

CAS

540-84-1

Other Names

• (CH3)2CHCH2C(CH3)3
• 2,2,4-Trimethylpentane
• ISOBUTYLTRIMETHYLMETHANE
• ISOOCTANE
• Isobutyltrimethylethane
• UN 1262

• ω : Acentric Factor.
• AP : Aniline Point (K).
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• η : Dynamic viscosity (Pa×s).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• R_g : Radius of Gyration.
• Δ_c,grossH : Heat of Combustion, Gross form (kJ/mol).
• Δ_c,netH : Heat of Combustion, Net Form (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).
• ν : Kinematic viscosity (m²/s).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• NFPA Fire : NFPA Fire Rating.
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_c : Critical density (kg/m³).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• c_sound,fluid : Speed of sound in fluid (m/s).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• λ : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• V_c : Critical Volume (m³/kmol).
• Z_c : Critical Compressibility.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Contents

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

Physical Properties

Property	Value	Unit	Source
ω	0.3030		KDB
AP	352.650	K	KDB
ΔcH°liquid	-5461.30 ± 1.30	kJ/mol	NIST
ΔfG°	13.69	kJ/mol	KDB
Rg	4.1710		KDB
Δc,grossH	5461.33	kJ/mol	KDB
Δc,netH	5065.192	kJ/mol	KDB
ΔfH°gas	[-224.30; -224.10]	kJ/mol
ΔfH°gas	-224.30	kJ/mol	KDB
ΔfH°gas	-224.10 ± 1.30	kJ/mol	NIST
ΔfH°liquid	-259.30 ± 1.30	kJ/mol	NIST
ΔfusH°	5.54	kJ/mol	Joback Calculated Property
ΔvapH°	[34.90; 35.24]	kJ/mol
ΔvapH°	35.24	kJ/mol	NIST
ΔvapH°	Outlier 34.90	kJ/mol	NIST
ΔvapH°	35.20 ± 0.10	kJ/mol	NIST
ΔvapH°	35.10 ± 0.10	kJ/mol	NIST
ΔvapH°	35.10	kJ/mol	NIST
ΔvapH°	35.10 ± 0.10	kJ/mol	NIST
ΔvapH°	35.12	kJ/mol	NIST
IE	[9.86; 9.91]	eV
IE	9.89 ± 0.03	eV	NIST
IE	9.91	eV	NIST
IE	9.86	eV	NIST
log10WS	[-4.74; -4.74]
log10WS	-4.74		Aq. Sol...
log10WS	-4.74		Estimat...
logPoct/wat	3.079		Crippen Calculated Property
McVol	123.580	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
Pc	[2564.33; 2583.79]	kPa
Pc	2570.00	kPa	KDB
Pc	2570.00	kPa	Critica...
Pc	2570.00 ± 20.00	kPa	NIST
Pc	2567.60 ± 40.53	kPa	NIST
Pc	2564.33 ± 10.13	kPa	NIST
Pc	Outlier 2583.79 ± 15.19	kPa	NIST
ρc	[243.31; 244.45]	kg/m3
ρc	244.45 ± 2.28	kg/m3	NIST
ρc	243.31 ± 4.57	kg/m3	NIST
ρc	243.31 ± 3.43	kg/m3	NIST
Inp	[680.00; 703.10]
Inp	692.70		NIST
Inp	689.10		NIST
Inp	694.00		NIST
Inp	691.10		NIST
Inp	689.90		NIST
Inp	690.20		NIST
Inp	690.60		NIST
Inp	693.00		NIST
Inp	Outlier 700.00		NIST
Inp	694.90		NIST
Inp	691.00		NIST
Inp	693.50		NIST
Inp	Outlier 697.70		NIST
Inp	Outlier 703.10		NIST
Inp	687.00		NIST
Inp	694.10		NIST
Inp	694.00		NIST
Inp	691.00		NIST
Inp	689.00		NIST
Inp	691.00		NIST
Inp	694.00		NIST
Inp	689.90		NIST
Inp	692.20		NIST
Inp	693.00		NIST
Inp	690.00		NIST
Inp	690.00		NIST
Inp	691.00		NIST
Inp	691.00		NIST
Inp	691.00		NIST
Inp	692.00		NIST
Inp	695.00		NIST
Inp	688.00		NIST
Inp	689.00		NIST
Inp	690.00		NIST
Inp	691.00		NIST
Inp	692.00		NIST
Inp	694.00		NIST
Inp	686.60		NIST
Inp	687.50		NIST
Inp	688.60		NIST
Inp	689.60		NIST
Inp	690.70		NIST
Inp	691.90		NIST
Inp	691.40		NIST
Inp	691.30		NIST
Inp	689.00		NIST
Inp	690.00		NIST
Inp	690.00		NIST
Inp	696.00		NIST
Inp	691.00		NIST
Inp	694.00		NIST
Inp	693.00		NIST
Inp	691.00		NIST
Inp	688.60		NIST
Inp	690.00		NIST
Inp	692.00		NIST
Inp	684.00		NIST
Inp	686.00		NIST
Inp	686.00		NIST
Inp	687.00		NIST
Inp	688.00		NIST
Inp	690.30		NIST
Inp	695.00		NIST
Inp	Outlier 699.00		NIST
Inp	687.00		NIST
Inp	694.00		NIST
Inp	689.00		NIST
Inp	689.00		NIST
Inp	688.00		NIST
Inp	690.00		NIST
Inp	692.00		NIST
Inp	694.00		NIST
Inp	688.00		NIST
Inp	690.00		NIST
Inp	688.00		NIST
Inp	690.00		NIST
Inp	692.00		NIST
Inp	696.00		NIST
Inp	687.00		NIST
Inp	689.00		NIST
Inp	689.00		NIST
Inp	692.00		NIST
Inp	691.00		NIST
Inp	693.00		NIST
Inp	694.00		NIST
Inp	687.00		NIST
Inp	694.00		NIST
Inp	690.00		NIST
Inp	Outlier 680.00		NIST
Inp	686.00		NIST
Inp	685.00		NIST
Inp	688.44		NIST
Inp	689.00		NIST
Inp	687.00		NIST
Inp	687.50		NIST
Inp	683.91		NIST
Inp	688.00		NIST
Inp	687.00		NIST
Inp	686.00		NIST
Inp	686.00		NIST
Inp	684.80		NIST
Inp	691.00		NIST
Inp	688.00		NIST
Inp	690.00		NIST
Inp	695.00		NIST
Inp	692.00		NIST
Inp	693.00		NIST
Inp	689.00		NIST
Inp	689.00		NIST
Inp	691.00		NIST
Inp	691.00		NIST
Inp	684.38		NIST
Inp	689.00		NIST
Inp	689.00		NIST
Inp	689.00		NIST
Inp	690.00		NIST
Inp	694.00		NIST
Inp	690.00		NIST
Inp	691.00		NIST
Inp	692.00		NIST
Inp	691.00		NIST
Inp	688.00		NIST
Inp	688.00		NIST
Inp	692.00		NIST
Inp	685.00		NIST
Inp	685.00		NIST
Inp	692.00		NIST
Inp	686.00		NIST
Inp	Outlier 700.00		NIST
Inp	Outlier 700.00		NIST
Inp	687.00		NIST
Inp	686.00		NIST
Inp	692.70		NIST
Inp	690.20		NIST
Inp	691.00		NIST
Inp	694.10		NIST
Inp	694.00		NIST
Inp	690.00		NIST
Inp	695.00		NIST
Inp	692.00		NIST
Inp	689.60		NIST
Inp	689.00		NIST
Inp	688.00		NIST
Inp	688.44		NIST
Inp	684.80		NIST
I	[676.00; 711.00]
I	676.00		NIST
I	698.00		NIST
I	711.00		NIST
I	705.00		NIST
I	711.00		NIST
S°liquid	[314.60; 328.03]	J/mol×K
S°liquid	328.03	J/mol×K	NIST
S°liquid	314.60	J/mol×K	NIST
Tboil	[371.45; 389.00]	K
Tboil	372.37	K	KDB
Tboil	372.33	K	Vapor l...
Tboil	372.33	K	Measure...
Tboil	372.26	K	Low-Pre...
Tboil	372.35	K	Vapor-L...
Tboil	372.40 ± 0.20	K	NIST
Tboil	372.40 ± 0.20	K	NIST
Tboil	372.40	K	NIST
Tboil	372.40	K	NIST
Tboil	372.00 ± 0.15	K	NIST
Tboil	372.40 ± 0.15	K	NIST
Tboil	372.50 ± 0.25	K	NIST
Tboil	372.30 ± 0.30	K	NIST
Tboil	372.15 ± 0.50	K	NIST
Tboil	372.30 ± 0.50	K	NIST
Tboil	372.35 ± 0.30	K	NIST
Tboil	372.39 ± 0.20	K	NIST
Tboil	371.45 ± 0.60	K	NIST
Tboil	372.15 ± 0.40	K	NIST
Tboil	372.30 ± 0.20	K	NIST
Tboil	372.40 ± 0.60	K	NIST
Tboil	372.37 ± 0.20	K	NIST
Tboil	372.38 ± 0.05	K	NIST
Tboil	372.39 ± 0.10	K	NIST
Tboil	372.65 ± 2.00	K	NIST
Tboil	372.15 ± 2.00	K	NIST
Tboil	372.35 ± 0.40	K	NIST
Tboil	372.45 ± 0.30	K	NIST
Tboil	372.50 ± 0.40	K	NIST
Tboil	372.38 ± 0.27	K	NIST
Tboil	372.38 ± 0.20	K	NIST
Tboil	372.38 ± 0.15	K	NIST
Tboil	372.45 ± 0.50	K	NIST
Tboil	372.38 ± 0.10	K	NIST
Tboil	372.38 ± 0.01	K	NIST
Tboil	372.39 ± 0.25	K	NIST
Tboil	372.38 ± 0.10	K	NIST
Tboil	372.45 ± 0.50	K	NIST
Tboil	372.39 ± 0.07	K	NIST
Tboil	372.50 ± 0.20	K	NIST
Tboil	372.55 ± 0.20	K	NIST
Tboil	372.39 ± 0.05	K	NIST
Tboil	372.38 ± 0.05	K	NIST
Tboil	372.39 ± 0.20	K	NIST
Tboil	372.55 ± 0.30	K	NIST
Tboil	372.38 ± 0.03	K	NIST
Tboil	372.25 ± 0.50	K	NIST
Tboil	372.25 ± 0.20	K	NIST
Tboil	372.38 ± 0.10	K	NIST
Tboil	372.38 ± 0.10	K	NIST
Tboil	372.40 ± 0.40	K	NIST
Tboil	372.25 ± 0.20	K	NIST
Tboil	372.65 ± 2.00	K	NIST
Tboil	372.35 ± 0.50	K	NIST
Tboil	372.45 ± 0.40	K	NIST
Tboil	372.45 ± 0.50	K	NIST
Tboil	Outlier 389.00 ± 2.00	K	NIST
Tc	[543.61; 544.30]	K
Tc	543.80	K	KDB
Tc	544.00	K	The Cri...
Tc	543.80 ± 0.30	K	NIST
Tc	543.90	K	NIST
Tc	543.89 ± 0.40	K	NIST
Tc	543.61 ± 0.20	K	NIST
Tc	543.82 ± 0.10	K	NIST
Tc	Outlier 544.30 ± 0.20	K	NIST
Tfus	[165.00; 166.15]	K
Tfus	165.80	K	KDB
Tfus	Outlier 166.07	K	Aq. Sol...
Tfus	165.78 ± 0.10	K	NIST
Tfus	165.75 ± 0.04	K	NIST
Tfus	165.76 ± 0.02	K	NIST
Tfus	165.75 ± 0.02	K	NIST
Tfus	165.76 ± 0.02	K	NIST
Tfus	165.73 ± 0.10	K	NIST
Tfus	165.73 ± 0.10	K	NIST
Tfus	165.73 ± 0.10	K	NIST
Tfus	165.73 ± 0.06	K	NIST
Tfus	165.73 ± 0.06	K	NIST
Tfus	165.73 ± 0.06	K	NIST
Tfus	165.77 ± 0.09	K	NIST
Tfus	165.77 ± 0.05	K	NIST
Tfus	165.76 ± 0.06	K	NIST
Tfus	165.76 ± 0.03	K	NIST
Tfus	165.85 ± 0.20	K	NIST
Tfus	165.73 ± 0.10	K	NIST
Tfus	165.76 ± 0.06	K	NIST
Tfus	165.75 ± 0.15	K	NIST
Tfus	165.76 ± 0.03	K	NIST
Tfus	165.77 ± 0.02	K	NIST
Tfus	165.73 ± 0.15	K	NIST
Tfus	165.75 ± 0.30	K	NIST
Tfus	165.75 ± 0.12	K	NIST
Tfus	165.77 ± 0.05	K	NIST
Tfus	165.78 ± 0.03	K	NIST
Tfus	165.75 ± 0.04	K	NIST
Tfus	165.77 ± 0.02	K	NIST
Tfus	165.78 ± 0.20	K	NIST
Tfus	165.75 ± 0.01	K	NIST
Tfus	165.83 ± 0.30	K	NIST
Tfus	165.83 ± 0.30	K	NIST
Tfus	165.75 ± 0.50	K	NIST
Tfus	165.78 ± 0.20	K	NIST
Tfus	165.78 ± 0.07	K	NIST
Tfus	165.55 ± 0.40	K	NIST
Tfus	165.83 ± 0.20	K	NIST
Tfus	165.55 ± 0.20	K	NIST
Tfus	165.84 ± 0.06	K	NIST
Tfus	Outlier 166.15 ± 2.00	K	NIST
Tfus	Outlier 165.00 ± 2.00	K	NIST
Tfus	165.65 ± 0.50	K	NIST
Tfus	165.45 ± 0.40	K	NIST
Tfus	Outlier 165.35 ± 0.50	K	NIST
Ttriple	[165.30; 165.76]	K
Ttriple	165.76 ± 0.40	K	NIST
Ttriple	165.30 ± 0.20	K	NIST
Vc	[0.468; 0.482]	m3/kmol
Vc	0.468	m3/kmol	KDB
Vc	0.468	m3/kmol	NIST
Vc	0.482 ± 0.020	m3/kmol	NIST
Zc	0.2660130		KDB
Zra	0.27		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[233.00; 313.27]	J/mol×K	[378.77; 557.09]
Cp,gas	233.00	J/mol×K	378.77	Joback Calculated Property
Cp,gas	248.05	J/mol×K	408.49	Joback Calculated Property
Cp,gas	262.39	J/mol×K	438.21	Joback Calculated Property
Cp,gas	276.06	J/mol×K	467.93	Joback Calculated Property
Cp,gas	289.08	J/mol×K	497.65	Joback Calculated Property
Cp,gas	301.48	J/mol×K	527.37	Joback Calculated Property
Cp,gas	313.27	J/mol×K	557.09	Joback Calculated Property
Cp,liquid	[233.70; 242.49]	J/mol×K	[293.15; 301.90]
Cp,liquid	237.85	J/mol×K	293.15	NIST
Cp,liquid	233.90	J/mol×K	295.20	NIST
Cp,liquid	242.49	J/mol×K	298.15	NIST
Cp,liquid	242.49	J/mol×K	298.15	NIST
Cp,liquid	239.71	J/mol×K	298.15	NIST
Cp,liquid	237.80	J/mol×K	298.15	NIST
Cp,liquid	237.80	J/mol×K	298.15	NIST
Cp,liquid	238.57	J/mol×K	298.15	NIST
Cp,liquid	238.87	J/mol×K	298.15	NIST
Cp,liquid	233.70	J/mol×K	300.00	NIST
Cp,liquid	241.00	J/mol×K	301.90	NIST
η	[0.0003690; 0.0005439]	Pa×s	[288.15; 323.15]
η	0.0005439	Pa×s	288.15	Densiti...
η	0.0005125	Pa×s	293.15	Densiti...
η	0.0004844	Pa×s	298.15	Densiti...
η	0.0004780	Pa×s	298.15	Densiti...
η	0.0004586	Pa×s	303.15	Densiti...
η	0.0004530	Pa×s	303.15	Densiti...
η	0.0004216	Pa×s	308.15	Densiti...
η	0.0004290	Pa×s	308.15	Densiti...
η	0.0004130	Pa×s	313.15	Densiti...
η	0.0004080	Pa×s	313.15	Densiti...
η	0.0003880	Pa×s	318.15	Densiti...
η	0.0003690	Pa×s	323.15	Densiti...
ΔfusH	[9.04; 9.21]	kJ/mol	[165.30; 165.80]
ΔfusH	9.04	kJ/mol	165.30	NIST
ΔfusH	9.04	kJ/mol	165.30	NIST
ΔfusH	9.04	kJ/mol	165.30	NIST
ΔfusH	9.21	kJ/mol	165.79	NIST
ΔfusH	9.20	kJ/mol	165.80	NIST
ΔvapH	[30.79; 40.70]	kJ/mol	[246.50; 517.00]
ΔvapH	40.70	kJ/mol	246.50	NIST
ΔvapH	36.10	kJ/mol	311.00	NIST
ΔvapH	34.40 ± 0.10	kJ/mol	313.00	NIST
ΔvapH	34.30 ± 0.10	kJ/mol	313.00	NIST
ΔvapH	33.40 ± 0.10	kJ/mol	328.00	NIST
ΔvapH	33.20 ± 0.10	kJ/mol	333.00	NIST
ΔvapH	34.80	kJ/mol	335.50	NIST
ΔvapH	32.60 ± 0.10	kJ/mol	343.00	NIST
ΔvapH	32.00 ± 0.10	kJ/mol	353.00	NIST
ΔvapH	31.70 ± 0.10	kJ/mol	358.00	NIST
ΔvapH	33.90	kJ/mol	358.50	NIST
ΔvapH	31.00 ± 0.10	kJ/mol	368.00	NIST
ΔvapH	31.00	kJ/mol	371.00	NIST
ΔvapH	31.01	kJ/mol	372.40	KDB
ΔvapH	30.79	kJ/mol	372.40	NIST
ΔvapH	32.20	kJ/mol	394.00	NIST
ΔvapH	31.50	kJ/mol	453.50	NIST
ΔvapH	31.60	kJ/mol	473.00	NIST
ΔvapH	31.40	kJ/mol	517.00	NIST
ν	[0.0000005; 0.0000007]	m2/s	[293.15; 323.15]
ν	0.0000007	m2/s	293.15	Density...
ν	0.0000007	m2/s	298.15	Density...
ν	0.0000007	m2/s	303.15	Density...
ν	0.0000006	m2/s	313.15	Density...
ν	0.0000005	m2/s	323.15	Density...
Pvap	[3.05; 282.80]	kPa	[283.60; 413.15]
Pvap	3.05	kPa	283.60	A milli...
Pvap	3.99	kPa	288.40	A milli...
Pvap	5.18	kPa	293.40	A milli...
Pvap	6.63	kPa	298.30	A milli...
Pvap	6.62	kPa	298.40	A milli...
Pvap	8.33	kPa	303.15	Measure...
Pvap	8.39	kPa	303.30	A milli...
Pvap	10.44	kPa	308.15	Measure...
Pvap	10.53	kPa	308.20	A milli...
Pvap	12.97	kPa	313.10	A milli...
Pvap	12.97	kPa	313.15	Measure...
Pvap	12.97	kPa	313.15	Thermod...
Pvap	12.95	kPa	313.15	Phase e...
Pvap	12.96	kPa	313.15	Vapor L...
Pvap	13.01	kPa	313.15	Vapor-L...
Pvap	12.95	kPa	313.15	Vapour-...
Pvap	15.96	kPa	318.10	A milli...
Pvap	15.98	kPa	318.15	Measure...
Pvap	19.54	kPa	323.00	A milli...
Pvap	19.54	kPa	323.15	Measure...
Pvap	20.00	kPa	323.65	Measure...
Pvap	23.81	kPa	328.00	A milli...
Pvap	28.66	kPa	332.80	A milli...
Pvap	100.05	kPa	371.55	Isobari...
Pvap	101.30	kPa	372.26	Low-Pre...
Pvap	101.30	kPa	372.33	Measure...
Pvap	101.33	kPa	372.35	Vapor-L...
Pvap	103.49	kPa	373.10	Phase E...
Pvap	104.94	kPa	373.40	Isobari...
Pvap	124.90	kPa	379.80	Isobari...
Pvap	149.96	kPa	386.94	Isobari...
Pvap	174.70	kPa	393.14	Isobari...
Pvap	199.94	kPa	398.64	Isobari...
Pvap	224.91	kPa	403.68	Isobari...
Pvap	249.95	kPa	408.28	Isobari...
Pvap	250.00	kPa	408.30	Isobari...
Pvap	282.80	kPa	413.15	Phase E...
n0	[1.37898; 1.39404]		[288.15; 318.15]
n0	1.39404		288.15	Densiti...
n0	1.39404		288.15	Densiti...
n0	1.38894		293.15	Isother...
n0	1.38921		298.10	Liquid-...
n0	1.38905		298.15	Volumet...
n0	1.38917		298.15	Liquid ...
n0	1.38898		298.15	Isother...
n0	1.38890		298.15	Phase e...
n0	1.38890		298.15	Excess ...
n0	1.38800		298.15	Excess ...
n0	1.38887		298.15	Vapor-L...
n0	1.38894		298.15	Isother...
n0	1.38890		298.15	(Vapor ...
n0	1.38900		298.15	Vapor l...
n0	1.38894		298.15	Isother...
n0	1.38904		298.15	(Vapour...
n0	1.38901		298.15	Volumet...
n0	1.38887		298.15	Vapor l...
n0	1.38920		298.15	Isother...
n0	1.38905		298.15	Measure...
n0	1.38902		298.15	Densiti...
n0	1.38887		298.15	Isobari...
n0	1.38900		298.15	Densiti...
n0	1.38900		298.15	Vapor-L...
n0	1.38898		298.15	Densiti...
n0	1.38900		298.15	Densiti...
n0	1.38900		298.15	A Study...
n0	1.38898		298.15	KDB
n0	1.38910		298.20	Vapor-L...
n0	1.38520		303.15	Excess ...
n0	1.38395		308.15	Densiti...
n0	1.38395		308.15	Densiti...
n0	1.38240		308.15	Excess ...
n0	1.38398		308.15	Densiti...
n0	1.37898		318.15	Densiti...
ρl	[649.40; 704.10]	kg/m3	[278.15; 343.15]
ρl	704.10	kg/m3	278.15	Advance...
ρl	700.05	kg/m3	283.15	Advance...
ρl	695.98	kg/m3	288.15	Advance...
ρl	691.88	kg/m3	293.00	Volumet...
ρl	692.00	kg/m3	293.00	KDB
ρl	691.83	kg/m3	293.15	Density...
ρl	692.05	kg/m3	293.15	Isother...
ρl	691.89	kg/m3	293.15	Advance...
ρl	691.91	kg/m3	293.15	Densiti...
ρl	692.00	kg/m3	293.15	Experim...
ρl	691.84	kg/m3	293.15	Density...
ρl	690.40	kg/m3	295.00	High-pr...
ρl	687.77	kg/m3	298.15	Thermod...
ρl	687.62	kg/m3	298.15	Excess ...
ρl	687.32	kg/m3	298.15	Liquid-...
ρl	687.76	kg/m3	298.15	Thermod...
ρl	687.81	kg/m3	298.15	Liquid ...
ρl	687.82	kg/m3	298.15	Densiti...
ρl	688.03	kg/m3	298.15	Excess ...
ρl	687.77	kg/m3	298.15	Advance...
ρl	687.82	kg/m3	298.15	Isobari...
ρl	688.18	kg/m3	298.15	Binary ...
ρl	687.91	kg/m3	298.15	Liquid ...
ρl	687.72	kg/m3	298.15	Phase e...
ρl	687.74	kg/m3	298.15	Density...
ρl	687.32	kg/m3	298.15	Thermod...
ρl	687.70	kg/m3	298.15	Density...
ρl	687.72	kg/m3	298.20	Apparen...
ρl	683.64	kg/m3	303.00	Volumet...
ρl	683.74	kg/m3	303.15	Isother...
ρl	683.59	kg/m3	303.15	Density...
ρl	683.64	kg/m3	303.15	Advance...
ρl	683.68	kg/m3	303.15	Densiti...
ρl	683.61	kg/m3	303.15	Density...
ρl	679.48	kg/m3	308.15	Advance...
ρl	679.40	kg/m3	308.15	Density...
ρl	679.47	kg/m3	308.15	Density...
ρl	679.51	kg/m3	308.15	Densiti...
ρl	675.30	kg/m3	313.00	Volumet...
ρl	675.29	kg/m3	313.15	Density...
ρl	675.23	kg/m3	313.15	Density...
ρl	675.28	kg/m3	313.15	Advance...
ρl	675.32	kg/m3	313.15	Densiti...
ρl	675.23	kg/m3	313.20	Apparen...
ρl	670.98	kg/m3	318.15	Density...
ρl	671.05	kg/m3	318.15	Densiti...
ρl	671.09	kg/m3	318.15	Density...
ρl	671.07	kg/m3	318.15	Advance...
ρl	666.84	kg/m3	323.00	Volumet...
ρl	666.80	kg/m3	323.15	Densiti...
ρl	666.81	kg/m3	323.15	Advance...
ρl	666.75	kg/m3	323.15	Density...
ρl	666.86	kg/m3	323.15	Density...
ρl	662.44	kg/m3	328.15	Density...
ρl	662.52	kg/m3	328.15	Advance...
ρl	658.20	kg/m3	333.15	Densiti...
ρl	658.16	kg/m3	333.15	Density...
ρl	658.19	kg/m3	333.15	Advance...
ρl	653.81	kg/m3	338.15	Advance...
ρl	653.80	kg/m3	338.15	Density...
ρl	649.40	kg/m3	343.15	Density...
ρl	649.44	kg/m3	343.15	Densiti...
ρl	649.40	kg/m3	343.15	Advance...
ΔfusS	[54.70; 55.56]	J/mol×K	[165.30; 165.79]
ΔfusS	54.70	J/mol×K	165.30	NIST
ΔfusS	55.56	J/mol×K	165.79	NIST
csound,fluid	[979.25; 1124.31]	m/s	[288.15; 323.15]
csound,fluid	1124.31	m/s	288.15	Tempera...
csound,fluid	1124.31	m/s	288.15	Influen...
csound,fluid	1113.83	m/s	290.65	Influen...
csound,fluid	1103.30	m/s	293.15	Influen...
csound,fluid	1092.66	m/s	295.65	Influen...
csound,fluid	1082.20	m/s	298.15	Influen...
csound,fluid	1082.20	m/s	298.15	Tempera...
csound,fluid	1071.72	m/s	300.65	Influen...
csound,fluid	1061.30	m/s	303.15	Influen...
csound,fluid	1050.89	m/s	305.65	Influen...
csound,fluid	1040.53	m/s	308.15	Influen...
csound,fluid	1030.22	m/s	310.65	Influen...
csound,fluid	1019.94	m/s	313.15	Influen...
csound,fluid	1009.71	m/s	315.65	Influen...
csound,fluid	999.53	m/s	318.15	Influen...
csound,fluid	989.37	m/s	320.65	Influen...
csound,fluid	979.25	m/s	323.15	Influen...
csound,fluid	979.25	m/s	323.15	Tempera...
γ	[0.02; 0.02]	N/m	[288.15; 323.15]
γ	0.02	N/m	288.15	Densiti...
γ	0.02	N/m	288.15	Surface...
γ	0.02	N/m	288.15	Densiti...
γ	0.02	N/m	298.15	Surface...
γ	0.02	N/m	298.15	Densiti...
γ	0.02	N/m	298.15	Densiti...
γ	0.02	N/m	298.20	KDB
γ	0.02	N/m	303.15	Surface...
γ	0.02	N/m	308.15	Densiti...
γ	0.02	N/m	308.15	Surface...
γ	0.02	N/m	308.15	Densiti...
γ	0.02	N/m	313.15	Surface...
γ	0.02	N/m	318.15	Surface...
γ	0.02	N/m	323.15	Surface...
λ	[0.09; 0.10]	W/m×K	[259.11; 328.14]
λ	0.10	W/m×K	259.11	Thermal...
λ	0.10	W/m×K	259.32	Thermal...
λ	0.10	W/m×K	259.52	Thermal...
λ	0.10	W/m×K	277.52	Thermal...
λ	0.10	W/m×K	277.74	Thermal...
λ	0.10	W/m×K	277.93	Thermal...
λ	0.10	W/m×K	295.67	Thermal...
λ	0.10	W/m×K	295.90	Thermal...
λ	0.10	W/m×K	296.10	Thermal...
λ	0.09	W/m×K	313.79	Thermal...
λ	0.09	W/m×K	314.02	Thermal...
λ	0.09	W/m×K	314.22	Thermal...
λ	0.09	W/m×K	327.69	Thermal...
λ	0.09	W/m×K	327.93	Thermal...
λ	0.09	W/m×K	328.14	Thermal...

Datasets

1. Viscosity, Pa*s (2)
2. Refractive index (Na D-line) (1)
3. Mass density, kg/m3 (1)
4. Speed of sound, m/s (2)
5. Thermal conductivity, W/m/K (1)

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
293.15	100.00	0.0005
293.15	1000.00	0.0005
293.15	5000.00	0.0005
293.15	10000.00	0.0006
293.15	20000.00	0.0006
293.15	30000.00	0.0007
293.15	40000.00	0.0008
293.15	50000.00	0.0009
293.15	60000.00	0.0010
293.15	70000.00	0.0010
293.15	80000.00	0.0011
293.15	100000.00	0.0013
293.15	120000.00	0.0015
293.15	140000.00	0.0017
298.15	100.00	0.0005
298.15	1000.00	0.0005
298.15	5000.00	0.0005
298.15	10000.00	0.0005
298.15	20000.00	0.0006
298.15	30000.00	0.0007
298.15	40000.00	0.0007
298.15	50000.00	0.0008
298.15	60000.00	0.0009
298.15	70000.00	0.0010
298.15	80000.00	0.0011
298.15	100000.00	0.0012
298.15	120000.00	0.0014
298.15	140000.00	0.0016
313.15	100.00	0.0004
313.15	1000.00	0.0004
313.15	5000.00	0.0004
313.15	10000.00	0.0005
313.15	20000.00	0.0005
313.15	30000.00	0.0006
313.15	40000.00	0.0006
313.15	50000.00	0.0007
313.15	60000.00	0.0008
313.15	70000.00	0.0008
313.15	80000.00	0.0009
313.15	100000.00	0.0010
313.15	120000.00	0.0012
313.15	140000.00	0.0014
323.15	100.00	0.0004
323.15	1000.00	0.0004
323.15	5000.00	0.0004
323.15	10000.00	0.0004
323.15	20000.00	0.0005
323.15	30000.00	0.0005
323.15	40000.00	0.0006
323.15	50000.00	0.0006
323.15	60000.00	0.0007
323.15	70000.00	0.0007
323.15	80000.00	0.0008
323.15	100000.00	0.0009
323.15	120000.00	0.0011
323.15	140000.00	0.0012
333.15	100.00	0.0003
333.15	1000.00	0.0003
333.15	5000.00	0.0004
333.15	10000.00	0.0004
333.15	20000.00	0.0004
333.15	30000.00	0.0005
333.15	40000.00	0.0005
333.15	50000.00	0.0006
333.15	60000.00	0.0006
333.15	70000.00	0.0007
333.15	80000.00	0.0007
333.15	100000.00	0.0008
333.15	120000.00	0.0010
333.15	140000.00	0.0011
348.15	100.00	0.0003
348.15	1000.00	0.0003
348.15	5000.00	0.0003
348.15	10000.00	0.0003
348.15	20000.00	0.0004
348.15	30000.00	0.0004
348.15	40000.00	0.0005
348.15	50000.00	0.0005
348.15	60000.00	0.0005
348.15	70000.00	0.0006
348.15	80000.00	0.0007
348.15	100000.00	0.0008
348.15	120000.00	0.0009
348.15	140000.00	0.0010
353.15	100.00	0.0003
353.15	1000.00	0.0003
353.15	5000.00	0.0003
353.15	10000.00	0.0003
353.15	20000.00	0.0004
353.15	30000.00	0.0004
353.15	40000.00	0.0004
353.15	50000.00	0.0005
353.15	60000.00	0.0005
353.15	70000.00	0.0006
353.15	80000.00	0.0006
353.15	100000.00	0.0007
353.15	120000.00	0.0008
353.15	140000.00	0.0009
Reference

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

Refractive index (Na D-line)

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Refractive index (Na D-line) - Liquid
298.15	101.33	1.3891
293.15	101.00	1.4211
303.15	101.00	1.416
313.15	101.00	1.4109
323.15	101.00	1.4055
293.15	101.00	1.3916
303.15	101.00	1.3866
313.15	101.00	1.3814
323.15	101.00	1.3763
Reference

Mass density, kg/m3

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
100.00	298.15	687.32
Reference

Speed of sound, m/s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Speed of sound, m/s - Liquid
294.06	100.00	1099.7
304.03	100.00	1058.5
313.81	100.00	1017.3
323.56	100.00	978.2
333.42	100.00	938.5
342.88	100.00	898.0
352.86	100.00	858.9
363.55	100.00	821.9
294.37	3000.00	1127.4
304.16	3000.00	1088.2
313.92	3000.00	1037.2
323.61	3000.00	999.1
333.48	3000.00	968.0
343.07	3000.00	927.9
352.89	3000.00	891.7
363.39	3000.00	852.2
373.04	3000.00	821.1
383.18	3000.00	783.2
393.83	3000.00	742.3
402.16	3000.00	716.5
412.57	3000.00	677.6
423.95	3000.00	636.8
434.51	3000.00	602.6
443.70	3000.00	569.7
452.94	3000.00	538.4
462.54	3000.00	502.1
472.45	3000.00	464.2
483.15	3000.00	423.5
493.12	3000.00	386.4
502.80	3000.00	350.1
512.41	3000.00	311.4
523.31	3000.00	264.5
294.65	6000.00	1147.6
304.23	6000.00	1109.6
313.96	6000.00	1065.2
323.65	6000.00	1027.4
333.50	6000.00	996.0
343.16	6000.00	954.8
352.94	6000.00	921.1
363.49	6000.00	883.5
373.27	6000.00	843.9
383.80	6000.00	813.8
394.00	6000.00	782.2
402.48	6000.00	750.9
412.84	6000.00	719.3
424.32	6000.00	678.1
434.94	6000.00	647.4
444.00	6000.00	619.6
453.22	6000.00	588.3
463.04	6000.00	558.9
472.86	6000.00	530.7
483.63	6000.00	496.7
493.56	6000.00	464.9
503.17	6000.00	435.4
513.04	6000.00	404.0
523.97	6000.00	371.4
294.84	10000.00	1176.1
304.27	10000.00	1136.9
313.82	10000.00	1100.1
323.67	10000.00	1060.4
333.46	10000.00	1028.0
343.22	10000.00	990.3
353.01	10000.00	961.7
363.54	10000.00	925.7
373.41	10000.00	888.2
384.11	10000.00	855.6
394.15	10000.00	825.8
402.64	10000.00	800.2
413.07	10000.00	766.7
424.49	10000.00	732.1
435.26	10000.00	701.0
444.22	10000.00	677.1
454.37	10000.00	648.8
463.43	10000.00	622.7
473.22	10000.00	596.3
484.05	10000.00	569.9
494.09	10000.00	542.2
503.79	10000.00	516.1
513.78	10000.00	491.8
524.59	10000.00	463.0
294.97	12000.00	1181.7
304.27	12000.00	1147.7
313.85	12000.00	1110.8
323.71	12000.00	1075.4
333.40	12000.00	1041.9
343.21	12000.00	1008.5
353.04	12000.00	975.5
363.58	12000.00	943.8
373.49	12000.00	908.6
384.26	12000.00	876.5
394.19	12000.00	848.1
402.78	12000.00	819.5
413.22	12000.00	791.3
424.59	12000.00	756.7
435.36	12000.00	726.5
444.36	12000.00	700.3
455.24	12000.00	671.1
463.72	12000.00	651.6
473.48	12000.00	627.7
484.30	12000.00	598.4
494.42	12000.00	576.5
504.09	12000.00	550.4
514.01	12000.00	526.6
524.70	12000.00	501.3
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Speed of sound, m/s - Liquid
100.00	293.15	1104.6
100.00	303.15	1061.7
100.00	313.15	1019.1
100.00	323.15	977.9
100.00	333.15	935.8
100.00	343.15	897.3
100.00	353.15	858.2
100.00	363.15	817.2
100.00	373.15	780.4
10000.00	293.15	1178.5
10000.00	303.15	1139.3
10000.00	313.15	1100.9
10000.00	323.15	1063.5
10000.00	333.15	1026.6
10000.00	343.15	992.6
10000.00	353.15	958.0
10000.00	363.15	924.3
10000.00	373.15	891.0
20000.00	293.15	1244.6
20000.00	303.15	1208.6
20000.00	313.15	1173.0
20000.00	323.15	1138.8
20000.00	333.15	1105.2
20000.00	343.15	1071.6
20000.00	353.15	1041.7
20000.00	363.15	1011.1
20000.00	373.15	980.7
30000.00	293.15	1304.8
30000.00	303.15	1270.2
30000.00	313.15	1237.0
30000.00	323.15	1204.7
30000.00	333.15	1173.0
30000.00	343.15	1142.7
30000.00	353.15	1114.1
30000.00	363.15	1085.5
30000.00	373.15	1057.5
40000.00	293.15	1358.5
40000.00	303.15	1326.8
40000.00	313.15	1295.2
40000.00	323.15	1264.6
40000.00	333.15	1234.2
40000.00	343.15	1205.7
40000.00	353.15	1178.7
40000.00	363.15	1151.4
40000.00	373.15	1125.2
50000.00	293.15	1410.3
50000.00	303.15	1378.5
50000.00	313.15	1349.3
50000.00	323.15	1319.0
50000.00	333.15	1290.2
50000.00	343.15	1262.9
50000.00	353.15	1236.1
50000.00	363.15	1211.3
50000.00	373.15	1185.9
60000.00	293.15	1458.1
60000.00	303.15	1427.0
60000.00	313.15	1397.6
60000.00	323.15	1369.8
60000.00	333.15	1341.8
60000.00	343.15	1315.4
60000.00	353.15	1290.4
60000.00	363.15	1265.7
60000.00	373.15	1242.1
70000.00	293.15	1502.5
70000.00	303.15	1472.6
70000.00	313.15	1443.4
70000.00	323.15	1416.6
70000.00	333.15	1390.0
70000.00	343.15	1363.5
70000.00	353.15	1339.5
70000.00	363.15	1316.6
70000.00	373.15	1293.1
80000.00	293.15	1544.7
80000.00	303.15	1515.6
80000.00	313.15	1487.6
80000.00	323.15	1461.2
80000.00	333.15	1434.9
80000.00	343.15	1410.8
80000.00	353.15	1386.8
80000.00	363.15	1364.4
80000.00	373.15	1341.5
90000.00	293.15	1584.5
90000.00	303.15	1556.4
90000.00	313.15	1529.0
90000.00	323.15	1503.4
90000.00	333.15	1479.0
90000.00	343.15	1453.6
90000.00	353.15	1431.0
90000.00	363.15	1408.2
90000.00	373.15	1386.0
100000.00	293.15	1622.6
100000.00	303.15	1594.5
100000.00	313.15	1568.7
100000.00	323.15	1543.4
100000.00	333.15	1519.0
100000.00	343.15	1495.3
100000.00	353.15	1472.5
100000.00	363.15	1449.9
100000.00	373.15	1428.5
110000.00	293.15	1658.9
110000.00	303.15	1632.1
110000.00	313.15	1605.9
110000.00	323.15	1581.4
110000.00	333.15	1557.7
110000.00	343.15	1534.0
110000.00	353.15	1512.1
110000.00	363.15	1490.6
110000.00	373.15	1469.2
120000.00	293.15	1694.0
120000.00	303.15	1667.5
120000.00	313.15	1641.7
120000.00	323.15	1617.8
120000.00	333.15	1594.1
120000.00	343.15	1571.7
120000.00	353.15	1549.6
120000.00	363.15	1529.0
120000.00	373.15	1508.2
130000.00	293.15	1727.5
130000.00	303.15	1701.6
130000.00	313.15	1676.3
130000.00	323.15	1653.1
130000.00	333.15	1629.5
130000.00	343.15	1607.2
130000.00	353.15	1585.9
130000.00	363.15	1565.5
130000.00	373.15	1545.1
140000.00	293.15	1760.1
140000.00	303.15	1734.3
140000.00	313.15	1709.4
140000.00	323.15	1686.4
140000.00	333.15	1663.5
140000.00	343.15	1641.7
140000.00	353.15	1620.5
140000.00	363.15	1600.8
140000.00	373.15	1580.3
150000.00	293.15	1791.1
150000.00	303.15	1766.4
150000.00	313.15	1741.7
150000.00	323.15	1718.6
150000.00	333.15	1696.2
150000.00	343.15	1675.0
150000.00	353.15	1654.1
150000.00	363.15	1634.2
150000.00	373.15	1614.0
Reference

Thermal conductivity, W/m/K

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Thermal conductivity, W/m/K - Liquid
254.60	100.00	0.1047
254.51	5000.00	0.1066
254.67	10100.00	0.1088
254.77	20000.00	0.1121
254.73	30000.00	0.1157
274.66	100.00	0.1004
274.63	5000.00	0.1021
274.61	10000.00	0.1041
274.61	20000.00	0.1080
274.57	30000.00	0.1114
295.33	100.00	0.0959
295.22	5000.00	0.0979
295.22	10100.00	0.1003
295.06	20100.00	0.1042
295.04	30100.00	0.1083
314.99	100.00	0.0907
314.85	5000.00	0.0930
314.87	10000.00	0.0953
314.93	20000.00	0.0996
314.91	29900.00	0.1038
334.53	100.00	0.0859
334.49	5100.00	0.0886
334.56	10000.00	0.0908
334.62	20000.00	0.0958
334.59	30000.00	0.0999
354.50	200.00	0.0817
354.78	5100.00	0.0843
354.83	10000.00	0.0868
354.73	20000.00	0.0915
354.80	30000.00	0.0960
374.63	400.00	0.0784
374.61	5000.00	0.0807
374.18	10000.00	0.0830
374.21	19900.00	0.0875
374.25	29900.00	0.0925
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.67]	kPa	[268.57; 398.53]	The Yaw...
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.40806e+01
Coefficient B			-3.12864e+03
Coefficient C			-4.17450e+01
Temperature range, min.			268.57
Temperature range, max.			398.53
Pvap	1.33	kPa	268.57	Calculated Property
Pvap	3.04	kPa	283.01	Calculated Property
Pvap	6.33	kPa	297.45	Calculated Property
Pvap	12.17	kPa	311.89	Calculated Property
Pvap	21.91	kPa	326.33	Calculated Property
Pvap	37.25	kPa	340.77	Calculated Property
Pvap	60.32	kPa	355.21	Calculated Property
Pvap	93.62	kPa	369.65	Calculated Property
Pvap	140.01	kPa	384.09	Calculated Property
Pvap	202.67	kPa	398.53	Calculated Property
Pvap	[1.48e-05; 2584.81]	kPa	[165.78; 543.96]	KDB Vap...
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			8.67458e+01
Coefficient B			-7.04177e+03
Coefficient C			-1.08858e+01
Coefficient D			8.87277e-06
Temperature range, min.			165.78
Temperature range, max.			543.96
Pvap	1.48e-05	kPa	165.78	Calculated Property
Pvap	7.82e-03	kPa	207.80	Calculated Property
Pvap	0.37	kPa	249.82	Calculated Property
Pvap	4.87	kPa	291.84	Calculated Property
Pvap	29.62	kPa	333.86	Calculated Property
Pvap	112.21	kPa	375.88	Calculated Property
Pvap	313.08	kPa	417.90	Calculated Property
Pvap	713.56	kPa	459.92	Calculated Property
Pvap	1420.70	kPa	501.94	Calculated Property
Pvap	2584.81	kPa	543.96	Calculated Property

Similar Compounds

Find more compounds similar to Pentane, 2,2,4-trimethyl-.

Mixtures

• Propane, 2-methoxy-2-methyl- + Pentane, 2,2,4-trimethyl-
• Diisopropyl ether + Pentane, 2,2,4-trimethyl-
• Methylal + Pentane, 2,2,4-trimethyl-
• Acetone + Pentane, 2,2,4-trimethyl-
• Ethanol + Pentane, 2,2,4-trimethyl-
• Ethanol + Acetone + Pentane, 2,2,4-trimethyl-
• Diisopropyl ether + Ethanol + Pentane, 2,2,4-trimethyl-
• 2-Butanone + Pentane, 2,2,4-trimethyl-
• 2-Butanone + Ethanol + Pentane, 2,2,4-trimethyl-
• Thiophene + Pentane, 2,2,4-trimethyl-
• 2-Butanone, 3-methyl- + Pentane, 2,2,4-trimethyl-
• Isopropyl Alcohol + Pentane, 2,2,4-trimethyl-
• 2-Butanone, 3-methyl- + Isopropyl Alcohol + Pentane, 2,2,4-trimethyl-
• 2-Pyrrolidinone, 1-methyl- + Pentane, 2,2,4-trimethyl-
• Carbonic acid, dimethyl ester + Pentane, 2,2,4-trimethyl-
• Carbonic acid, dimethyl ester + Ethanol + Pentane, 2,2,4-trimethyl-
• Thiophene, 3-methyl- + Pentane, 2,2,4-trimethyl-
• 1-Butanethiol + Pentane, 2,2,4-trimethyl-
• Disulfide, dimethyl + Pentane, 2,2,4-trimethyl-
• Diethyl disulfide + Pentane, 2,2,4-trimethyl-

Find more mixtures with Pentane, 2,2,4-trimethyl-.

Sources

• KDB Pure (Korean Thermophysical Properties Databank)
• KDB Vapor Pressure Data
• Crippen Method
• Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
• Liquid liquid equilibria for pseudoternary systems: isooctane benzene (methanol +water)
• Phase equilibria for binary systems of octane boosters with 2,2,4-trimethylpentane
• Isobaric vapor liquid equilibria for mixtures of acetone, ethanol, and 2,2,4-trimethylpentane at 101.3 kPa
• Solubility of CO2 in branched alkanes in order to extend the PPR78 model (predictive 1978, Peng Robinson EOS with temperature-dependent kij calculated through a group contribution method) to such systems
• Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent
• Vapor liquid equilibria for binary and ternary mixtures of diisopropyl ether, ethanol, and 2,2,4-trimethylpentane at 101.3 kPa
• Vapor liquid equilibria for binary and ternary mixtures of ethanol, 2-butanone, and 2,2,4-trimethylpentane at 101.3 kPa
• 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
• Isothermal vapor liquid equilibrium at 303.15K and excess molar volumes at 298.15 K for the ternary system of propyl vinyl ether + 1-propanol + 2,2,4-trimethyl-pentane and its binary sub-systems
• Isothermal vapour liquid equilibria in the binary and ternary systems composed of 2-propanol, 3-methyl-2-butanone and 2,2,4-trimethylpentane
• Measurement and prediction of pyrene solubility in pure, binary, ternary and quaternary solvent systems
• Liquid liquid equilibria of lactam containing binary systems
• Solubility of hydrocarbons in water: Experimental measurements and modeling using a group contribution with association equation of state (GCA-EoS)
• Isothermal vapor liquid equilibrium at 333.15K and excess molar volumes and refractive indices at 298.15K for the mixtures of di-methyl carbonate, ethanol and 2,2,4-trimethylpentane
• Phase equilibria on four binary systems containing 3-methylthiophene
• Isothermal vapor liquid equilibrium at 333.15K, excess molar volumes and refractive indices at 298.15K for mixtures of tert-amyl methyl ether + ethanol + 2,2,4-trimethylpentane
• (Liquid + liquid) equilibria of the quaternary sysytem methanol + isooctane + cyclohexane + benzene at T = 303.15 K
• Excess enthalpies of oxygenated compounds + hydrocarbon mixtures: Binary and ternary mixtures containing dibutyl ether (DBE), 1-butanol and 2,2,4-trimethylpentane at 298.15 K
• Phase equilibrium for the systems diisopropyl ether, isopropyl alcohol + 2,2,4-trimethylpentane and + n-heptane at 101.3 kPa
• Measurements of different thermodynamic properties of systems containing ionic liquids and correlation of these properties using modified UNIFAC (Dortmund)
• Phase equilibria on five binary systems containing 1-butanethiol and 3-methylthiophene in hydrocarbons
• Phase equilibria for systems containing dimethyl disulfide and diethyl disulfide with hydrocarbons at 368.15 K
• Vapor liquid equilibrium for binary system of tetrahydrothiophene + 2,2,4-trimethylpentane and tetrahydrothiophene + 2,4,4-trimethyl-1-pentene at 358.15 and 368.15 K
• Infinite dilution activity coefficient and vapour liquid equilibrium measurements for dimethylsulphide and tetrahydrothiophene with hydrocarbons
• Volumetric behavior of the binary systems benzene + cyclohexane and benzene + 2,2,4-trimethyl-pentane at temperatures 293.15-323.15K
• Measurements and correlation of vapour liquid equilibria of 2-butanone and hydrocarbons binary systems at two different pressures
• Isothermal vapour-liquid equilibria in the binary and ternary systems composed of 2,2,4-trimethylpentane, 2-methyl-1-propanol, and 4-methyl-2-pentanone
• Ether + alcohol + hydrocarbon mixtures in fuels and bio-fuels: Excess enthalpies of binary mixtures containing dibutyl ether (DBE) or 1-butanol and 1-hexene or methylcyclohexane or toluene or cyclohexane or 2,2,4-trimethylpentane at 298.15K and 313.15K
• Liquid-liquid equilibria of mixtures with ethyl lactate and various hydrocarbons
• Activity coefficients at infinite dilution of organic solutes in 1-octyl-3-methylimidazolium nitrate using gas-liquid chromatography
• (Liquid + liquid) equilibria for the ternary system of (N-formylmorpholine + ethylbenzene + 2,2,4-trimethylpentane) at temperatures (303.15, 313.15, and 323.15) K
• Excess molar volumes, excess molar enthalpies and refractive index deviations for binary mixtures of propan-1-ol, butan-1-ol and pentan-1-ol with 2,2,4-trimethylpentane at 298.15 K
• Volumetric behavior of the ternary system benzene-2-methoxy-2-methylbutane-2,2,4-trimethylpentane and all binary sub-systems at temperature range (298.15 - 318.15) K
• Vapour liquid equilibria and excess enthalpies of the binary mixtures 1-pentanol with 2,2,4-trimethylpentane or n-heptane
• The liquid-liquid coexistence curves of {x nitrobenzene + (1 - x) 2-methylpentane} and {x nitrobenzene + (1 - x) isooctane} in the critical region
• Towards automated characterisation of liquid-liquid equilibria
• Phase equilibrium properties of binary and ternary mixtures containing 2-butanol, 2,2,4- trimethylpentane and 1-hexene at 313.15 K
• Thermodynamic behaviour of second generation biofuels: Vapour liquid equilibria and excess enthalpies of the binary mixtures 2-pentanol and n-heptane or 2,2,4-trimethylpentane
• Study of interaction between organic compounds and mono or dicationic oxygenated ionic liquids using gas chromatography
• High-pressure vapor-liquid equilibria of the second generation biofuel blends (2-methylfuran + iso-octane) and (2-methyltetrahydrofuran + di-n-butyl ether): Experiments and PCP-SAFT modeling
• Vapour-liquid equilibria of the ternary mixture (1-pentanol + 2,2,4-trimethylpentane + heptane) and the binary mixture (2,2,4-trimethylpentane + heptane) at T = 313.15 K for the characterization of second generation biofuels.
• 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
• Thermodynamics of aromatic polar compound (alkanone, alkanal or alkanoate) + hydrocarbon mixtures
• A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
• 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
• Isobaric vapor-liquid equilibrium, density and speed of sound of binary mixtures 2,2,4-trimethylpentane + 1-butanol or dibutyl ether (DBE) at 101.3 kPa
• 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
• The pressure dependence of viscosity for 2,2,4 trimethylhexane to 1 GPa along the 20 C isotherm
• Excess enthalpies of binary mixtures of 1-hexene with some branched alkanes at the temperature 298.15 K
• Excess molar enthalpies of the ternary mixtures: (methyl tert-butyl ether or 2-methyltetrahydrofuran + cyclohexane + 2,2,4- trimethylpentane} at the temperature 298.15 K
• Excess properties of the binary mixtures of methylcyclohexane + alkanes (C6 to C12) at T = 298.15 K to T = 308.15 K
• (Vapor + liquid) equilibria of binary mixtures formed by iso-octane with a variety of compounds at 95.8 kPa
• Temperature influence on mixing properties of {ethyl tert-butyl ether (ETBE) + gasoline additives}
• Volumetric behaviour of binary liquid systems composed of toluene, isooctane, and methyl tert-butyl ether at temperatures from (298.15 to 328.15) K
• Evaluation of the polysubstituted pyridinium ionic liquid [hmmpy][Ntf2] as a suitable solvent for desulfurization: Phase equilibria
• Volumetric behaviour of the ternary liquid system composed of methyl tert-butyl ether, toluene, and isooctane at temperatures from (298.15 to 328.15) K: Experimental data and correlation
• Densities, viscosities, refractive indices, and surface tensions for binary and ternary mixtures of 2-propanol, tetrahydropyran, and 2,2,4-trimethylpentane
• 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
• Volumetric behaviour of binary and ternary liquid systems composed of ethanol, isooctane, and toluene at temperatures from (298.15 to 328.15) K. Experimental data and correlation
• Isothermal (vapour + liquid) equilibria in the binary and ternary systems composed of 2-propanol, 2,2,4-trimethylpentane, and 2,4-dimethyl-3-pentanone
• (Liquid + liquid) equilibrium for binary systems of N-formylmorpholine with alkanes
• (Vapour + liquid) equilibria for binary and ternary mixtures of 2-propanol, tetrahydropyran, and 2,2,4-trimethylpentane at P = 101.3 kPa
• 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
• The potential of head-space gas chromatography for VLE measurements
• 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
• Densities and viscosities of binary and ternary mixtures of cyclohexanone, 1,4-dioxane and isooctane from T = (288.15 to 313.15) K
• 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 coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds: Saturated fatty acids
• 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
• Advanced calibration, adjustment, and operation of a density and sound speed analyzer
• Physicochemical properties and activity coefficients at infinite dilution for organic solutes and water in a novel bicyclic guanidinium superbase-derived protic ionic liquid
• Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds Part II: C18 fatty acids
• 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
• Vapour-liquid equilibria of binary and ternary mixtures containing 1-butanol, 2,2,4-trimethylpentane and 1-hexene at T = 313.15 K
• 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
• Volumetric behaviour of the (2,2,4-trimethylpentane + methylbenzene + butan-1-ol) ternary system and its binary sub-systems within the temperature range (298.15-328.15) K
• 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
• Activity coefficients at infinite dilution of organic solutes in 1-hexyl-3- methylimidazolium trifluoroacetate and influence of interfacial adsorption using gas liquid chromatography
• Application of 1-pentyl-3-methylimidazolium bis(trifluoromethylsulfonyl) imide for desulfurization, denitrification and dearomatization of FCC gasoline
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-butyl-3-methylimidazolium methyl sulfate
• Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
• 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
• Activity coefficients at infinite dilution of alkanes, alkenes, alkyl benzenes in dimethylphosphate based ionic liquids using gas liquid chromatography
• Contributing to accurate high pressure viscosity measurements: Vibrating wire viscometer and falling body viscometer techniques
• 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
• Viscosities of binary mixtures containing 1-butanol + 2,2,4-trimethylpentane or + 1,2,4-trimethylbenzene at high pressures for the thermophysical characterization of biofuels
• 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
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
• Thermodynamics and activity coefficients at infinite dilution for organic compounds and water in the ionic liquid 1-butyl-3-methylimidazolium perchlorate
• Thermodynamics of mixtures containing aromatic nitriles
• 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
• Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in ionic liquid [HMMIM][BF4]
• Viscosities of binary mixtures containing 2-butanol + hydrocarbons (2,2,4-trimethylpentane or 1,2,4-trimethylbenzene) at high pressures for the implementation of second generation biofuels
• The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
• Thermodynamics and activity coefficients at infinite dilution for organic compounds in the ionic liquid 1-hexyl-3-methylimidazolium chloride
• Separation of binary mixtures based on gamma infinity data using [OMMIM][BF4] ionic liquid and modelling of thermodynamic functions
• Determination of the thermodynamic parameters of ionic liquid 1-propyl-3-methylimidazolium bromide by gas-liquid chromatography
• Separation of (water/butan-1-ol) binary systems based on activity coefficients at infinite dilution with phosphonium ionic liquid
• Excess volumes, densities, speeds of sound and viscosities for the binary systems of diisopropyl ether with hydrocarbons at 303.15K
• Density and Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane + n-Heptane, 2,2,4-Trimethylpentane + n-Octane, Ethyl Acetate + Benzene, and Butanenitrile + Benzene from (293.15 to 323.15) K
• Densities, Viscosities, Refractive Indices, and Surface Tensions of Binary Mixtures of 2,2,4-Trimethylpentane with Several Alkylated Cyclohexanes from (293.15 to 343.15) K
• A Study on Alkane + Ester + Ester Systems. Physicochemical Behavior of Binaries and Ternaries of Octane or Iso-octane with Methyl Esters (Ethanoate, Butanoate, Pentanoate)
• Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
• 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, Equilibrium Phase Densities, and Refractive Indices for the Quaternary Mixtures Containing 2-Propanol or 2-Methyl-2-Propanol of Fuel Oxygenate at T = 298.15 and 318.15 K
• Solubility of 2-Ethylanthraquinone in Binary Mixtures of Oligooxymethylene Dimethyl Ethers with Different Number of CH2O Groups of n = 2, 3, and 4 from 293.15 to 343.15 K
• Influence of Temperature on the Liquid Liquid Phase Equilibria of Ternary (Water + Alcohol + Entrainer) Systems
• The Critical Temperatures of a Number of (i) (Chloroalkane (C3 C4) + Hydrocarbon (C6 C7)) Binary Mixtures and (ii) (Aromatic Halocarbon (Chlorobenzene, Fluorobenzene, 1,2-Dichlorobenzene, or 1,3-Dichlorobenzene) + Alkane (C8)) Binary Mixtures
• Measurement and Correlation of Isothermal Binary Vapor Liquid Equilibrium for Diethyl Carbonate + Isooctane/n-Heptane/Toluene Systems
• High Pressure Volumetric Properties of the Binary Mixtures Di-isopropyl Ether + 2,2,4-Trimethylpentane
• Experimental Solubility Data for Binary Mixtures of Ethane and 2,2,4-Trimethylpentane at Pressures up to 6 MPa Using a New Variable-Volume Sapphire Cell
• Measurements of the Speed of Sound in Liquid and Supercritical n-Octane and Isooctane
• Liquid-Liquid Equilibria for 2-Phenylethan-1-ol + Alkane Systems
• Solubility Measurement and Thermodynamic Modeling of Benzoic Acid in Monosolvents and Binary Mixtures
• Solubility Measurement and Correlation for epsilon-2,4,6,8,10,12-Hexanitro-2,4,6,8,10,12-hexaazaisowurtzitane in Different Alkanes/Aromatic Hydrocarbon + Ethyl Acetate Binary Solvents at Temperatures of between 283.15 and 323.15 K
• Vapor-Liquid Equilibrium Measurements of Ether Alcohol Blends for Investigation on Reformulated Gas
• Determination of Activity Coefficients at Infinite Dilution of Solutes in N,N'-Di(2-ethylhexyl)isobutyramide Using Inverse Gas-Liquid Chromatography
• Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
• Solubilities of 2,6-Dimethylnaphthalene in Six Pure Solvents and Two Binary Solvent Systems
• Measurements of the Thermal Conductivity of n-Octane, Isooctane, 1-Octene, and 1-Octanol in the Temperature Range from 253 to 393 K at Pressures up to 30 MPa
• Measurement of VLE Data by Using an Experimental Installation with Automatic Control: Modeling of Binary Systems of Methyl Acetate or Ethyl Acetate with n-Heptane or 2,2,4-Trimethylpentane at Both 0.1 and 1.5 MPa
• Effect of Composition and Temperature upon Density, Viscosity, Surface Tension, and Refractive Index of 2,2,4-Trimethylpentane + Cyclohexane + Decane Ternary Liquid Systems
• Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
• Isobaric Vapor-Liquid and Vapor-Liquid-Liquid Equilibria Data for the System Water + Isopropanol + Isooctane
• Liquid-Liquid Equilibria for Monoethylene Glycol + Water + Alkane Systems in the Range (273 to 313) K and Atmospheric Pressure
• Phase Separation in Binary Mixtures Containing Linear Perfluoroalkanes
• Densities and Viscosities for Binary and Ternary Mixtures of Ethanol, 2-Butanone, and 2,2,4-Trimethylpentane at T = (298.15, 308.15, and 318.15) K
• Densities, Refractive indices and Viscosities for Binary and Ternary Mixtures of Acetone, Ethanol and 2,2,4-Trimethylpentane at T = (288.15, 298.15, and 308.15) K
• Densities, Viscosities, and Refractive Indices for Binary and Ternary Mixtures of Ethanol, 2-Methylpropan-2-ol, and 2,2,4-Trimethylpentane
• Speed of Sound of 2-Methylpentane, 2,3-Dimethylpentane, and 2,2,4-Trimethylpentane from (293.15 to 373.15) K and up to 150 MPa
• Density, Viscosity, and Speed of Sound of Solutions of AOT Reverse Micelles in 2,2,4-Trimethylpentane
• Densities, Viscosities, and Refractive Indices for Binary and Ternary Mixtures of Diisopropyl Ether, Ethanol, and 2,2,4-Trimethylpentane
• Phase Equilibria on Four Binary Systems: 1,2-Dichloroethane + trans-1,2-Dichloroethylene, 1-Octene + 2-Methyl Thiophene, 2-Ethyl Thiophene + 2,2,4-Trimethylpentane, and Cyclopropanecarbonitrile + Water
• (Liquid + Liquid) Equilibria of Oxygenate Fuel Additives with Water: (Water + Diisopropyl Ether + 2,2,4-Trimethylpentane + Ethanol) and (Water + Diisopropyl Ether + 2,2,4-Trimethylpentane + 2-Propanol)
• Activity Coefficients at Infinite Dilution in 1-Alkyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
• Vapor-Liquid Equilibrium of Ferrocene in Some Organic Solvents Using Spectroscopic Methods
• Vapor-Liquid Equilibrium of Binary Mixtures. 2. Ethanol + 2,2,4-Trimethylpentane, 1-Butanol + 2,2,4-Trimethylpentane, and Ethanol + o-Xylene
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Density, Speed of Sound, Surface Tension, and Refractive Index of AOT + 2,2,4-Trimethylpentane + Water Mixtures from (5 to 60) deg C
• Excess Molar Volumes at 298.15 K and Isothermal Vapor-Liquid Equilibria at 333.15 K for the Binary Mixtures of Dimethyl Carbonate with Benzene, Toluene, n-Heptane, and Isooctane
• Solubility of Ethylene in 2,2,4-Trimethylpentane at Various Temperatures and Pressures
• Vapor-Liquid Equilibrium for Binary System of Diethyl Sulfide + n-Heptane and Diethyl Sulfide + 2,2,4-Trimethylpentane at (363.15 and 353.15) K
• Solubility of Anthracene in Binary Diisopropyl Ether + Alkane Solvent Mixtures at 298.15 K
• Measurement and Modeling of Liquid-Liquid Equilibrium for Ternary and Quaternary Mixtures of Water, Methanol, 2-Propanol, and 2,2,4-Trimethylpentane at 293.2 K
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Decyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Activity Coefficients at Infinite Dilution in Methylimidazolium Nitrate Ionic Liquids
• Solubility of Anthracene and Phenanthrene in Ethanol + 2,2,4-Trimethylpentane Mixtures at Different Temperatures
• Activity Coefficients at Infinite Dilution of Organic Compounds in Four New Imidazolium-Based Ionic Liquids
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Ethyl-3-methylimidazolium Diethylphosphate Using Gas Liquid Chromatography
• Isothermal Vapor Liquid Equilibrium Data of Propan-1-ol + 2,2,4-Trimethylpentane and Butan-1-ol + 2,2,4-Trimethylpentane at 318.15 K
• Apparent and Partial Molar Volumes at Infinite Dilution and Solid Liquid Equilibria of Dibenzothiophene + Alkane Systems
• Measurement and Calculation of Liquid Liquid Equilibria of Ternary and Quaternary Systems Containing Water, Propan-1-ol, and 2,2,4-Trimethylpentane (TMP) with 2,2'-Oxybis(propane) (DIPE) or Dimethyl Carbonate (DMC)
• Partition Coefficients of Organic Compounds in Four New Tetraalkylammonium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Using Inverse Gas Chromatography
• Vapor-Liquid Equilibria of Binary Mixtures Containing 1-Butanol and Hydrocarbons at 313.15 K
• Evaluation of the Performance of Trigeminal Tricationic Ionic Liquids for Separation Problems
• Excess Volumes of Ternary Mixtures 2,2,4-Trimethylpentane + Diisopropyl Ether or Methyl tert-Butyl Ether + Methanol, Ethanol, or 1-Propanol at 298.15 K
• Vapor Liquid Equilibria of Binary Mixtures Containing 2-Butanol and Hydrocarbons at 313.15 K
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Dibutylphosphate Using Gas Liquid Chromatography
• Vapor Liquid Liquid Equilibria Measurements for the Dehydration of Ethanol, Isopropanol, and n-Propanol via Azeotropic Distillation Using DIPE and Isooctane as Entrainers
• Liquid Liquid Equilibria for Dipropylene Glycol Hydrocarbon Binary Systems: Experimental Data and Regression
• 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
• Thermodynamics of Mixtures Containing a Very Strongly Polar Compound. 10. Liquid Liquid Equilibria for N,N-Dimethylacetamide + Selected Alkanes
• Isobaric Vapor Liquid Equilibrium for Binary Systems of 2,2,4-Trimethylpentane with o-Xylene, m-Xylene, p-Xylene, and Ethylbenzene at 250 kPa
• Infinite Dilution Activity Coefficients of Solutes Dissolved in Two Trihexyl(tetradecyl)phosphonium Ionic Liquids
• Oxygenated Compounds + Hydrocarbon Mixtures in Fuels and Biofuels: Excess Enthalpies of Ternary Mixtures Containing 1-Butoxybutane + Propan-1-ol +1-Hex-1-ene, or Heptane, or 2,2,4-Trimethylpentane at (298.15 and 313.15) K
• Density, Viscosity, Speed of Sound, Bulk Modulus, and Surface Tension of Binary Mixtures of n-Heptane + 2,2,4-Trimethylpentane at (293.15 to 338.15) K and 0.1 MPa
• Densities and Viscosities of Binary Mixtures of 2,2,4-Trimethylpentane + 1-Propanol, + 1-Pentanol, + 1-Hexanol, and + 1-Heptanol from (298.15 to 323.15) K
• Deduction of Physicochemical Properties from Solubilities: 2,4-Dihydroxybenzophenone, Biotin, and Caprolactam as Examples
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Propyl-2,3-dimethylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Isothermal Binary and Ternary VLE for the Mixtures of Propyl Vinyl Ether + Ethanol + Isooctane at 323.15 K and VE at 293.15 K
• Critical Temperatures and Pressures of Several Binary and Ternary Mixtures Concerning the Alkylation of 2-Methylpropane with 1-Butene in the Presence of Methane or Carbon Dioxide
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas-Liquid Chromatography
• Binary LLE for Propyl Vinyl Ether (PVE) + Water, Ternary LLE for PVE + Methanol or Ethanol + Water at 298.15 K, and VE and centsR at 293.15 K for the Mixture of PVE + Ethanol + 2,2,4-Trimethylpentane
• Isothermal VLE and VE at 303.15 K for the Binary and Ternary Mixtures of Di-isopropyl Ether (DIPE) + 1-Propanol + 2,2,4-Trimethylpentane
• Naphthalene Solubility in Binary Solvent Mixtures of 2,2,4-Trimethylpentane + Alcohols at 298.15 K
• Liquid Liquid Equilibrium for Ternary Systems of Propyl Vinyl Ether + C3 or C4 Alcohols + Water at 298.15 K and Excess Molar Enthalpies for Ternary and Constituent Binary Systems of Propyl Vinyl Ether + Ethanol + Isooctane at 303.15 K
• Densities, Viscosities, Refractive Indexes, and Surface Tensions for Binary and Ternary Mixtures of Tetrahydofuran, 2-Propanol, and 2,2,4-Trimethylpentane
• Measurements and Correlation of Liquid Liquid Equilibria of (Water + Ethanol + Dimethyl Carbonate + 2,2,4-Trimethylpentane or n-Heptane) and (Water + Dimethyl Carbonate + n-Heptane + Toluene)
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Hexyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas-Liquid Chromatography
• Solubility of CO2, N2, and CO2 + N2 Gas Mixtures in Isooctane
• Liquid-Liquid Equilibria for [C8mim][NTf2] + Thiophene + 2,2,4-Trimethylpentane or + Toluene
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Ethyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Inverse Gas Chromatography
• Densities, Viscosities, Refractive Indices, and Surface Tensions for the Mixtures of 1,3-Dioxolane + 2-Propanol or + 2,2,4-Trimethylpentane at (288.15, 298.15, and 308.15) K and 1,3-Dioxolane + 2-Propanol + 2,2,4-Trimethylpentane at 298.15 K
• Isothermal Vapor-Liquid Equilibrium at 333.15 K and Excess Molar Volumes, Refractive Indices, and Excess Molar Enthalpies at 303.15 K for the Binary and Ternary Mixtures of Di-isopropyl Ether, Ethanol, and 2,2,4-Trimethylpentane
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-(2-Hydroxyethyl)-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Liquid-Liquid Equilibria for Monoethylene Glycol + Hexane and 2,2,4-Trimethylpentane, Water + Hexane and 2,2,4-Trimethylpentane, Monoethylene Glycol + Water + Hexane, and Monoethylene Glycol + Water + 2,2,4-Trimethylpentane in the Temperature Range between T = 283.15 K and T = 323.15 K
• Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
• Vapor-Liquid Equilibria for Binary and Ternary Mixtures of 1,3-Dioxolane, 2-Propanol, and 2,2,4-Trimethylpentane at 101.3 kPa
• Comparison of the Efficiencies of Amine Extractants on Lactic Acid with Different Organic Solvents
• Isothermal Vapor-Liquid Equilibrium at 333.15 K and Excess Volumes and Molar Refractivity Deviation at 298.15 K for Binary System Dibutyl Ether (DBE) + 2,2,4-Trimethylpentane and for Ternary System DBE + Ethanol + 2,2,4-Trimethylpentane
• Isobaric Vapor-Liquid-Liquid Equilibrium and Vapor-Liquid Equilibrium for the Quaternary System Water-Ethanol-Cyclohexane-Isooctane at 101.3 kPa
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in Glycerol Using Gas-Liquid Chromatography
• Thermodynamics of Mixtures Containing a Strongly Polar Compound. 9. Liquid-Liquid Equilibria for epsilon-Caprolactam + Selected Alkanes
• Study of Ether-, Alcohol-, or Cyano-Functionalized Ionic Liquids Using Inverse Gas Chromatography
• Isothermal Vapor-Liquid Equilibria in the Two Binary and the Ternary Systems Composed of tert-Amyl Methyl Ether, tert-Butanol, and Isooctane
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more. Take the time to validate and double check the source of the data.
Outlier This icon means that the value is more than 2 standard deviations away from the property mean.