Chemical Properties of 2-Propanol, 2-methyl- (CAS 75-65-0)

InChI

InChI=1S/C4H10O/c1-4(2,3)5/h5H,1-3H3

InChI Key

DKGAVHZHDRPRBM-UHFFFAOYSA-N

Formula

C4H10O

SMILES

CC(C)(C)O

Molecular Weight¹

74.12

CAS

75-65-0

Other Names

• 1,1-Dimethylethanol
• 2-METHYL-2-PROPANOL
• 2-Methyl n-propan-2-ol
• 2-Methylpropan-2-ol
• 2-Methylpropanol-2
• Alcool butylique tertiaire
• Butanol tertiaire
• Ethanol, 1,1-Dimethyl-
• Methanol, trimethyl-
• Methyl-2 propanol-2
• NCI-C55367
• TERT-BUTANOL
• TERT-BUTYL ALCOHOL
• TRIMETHYLMETHANOL
• Tert.-butyl alcohol
• Trimethylcarbinol
• t-Butanol
• t-Butyl hydroxide
• tert-Butyl hydroxide
• tert-C4H9OH

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• T_ig : Autoignition Temperature (K).
• BasG : Gas basicity (kJ/mol).
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• Δ_cH°_solid : Standard solid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• C_p,solid : Solid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• LFL : Lower Flammability Limit (% in Air).
• UFL : Upper Flammability Limit (% in Air).
• T_flash,cc : Flash Point (Closed Cup Method) (K).
• T_flash,oc : Flash Point (Open Cup Method) (K).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• R_g : Radius of Gyration.
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_subH° : Enthalpy of sublimation at standard conditions (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).
• 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.
• NFPA Health : NFPA Health 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).
• S°_{solid,1 bar} : Solid phase molar entropy at standard conditions (J/mol×K).
• 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.
• 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	0.6120		KDB
PAff	802.60	kJ/mol	NIST
Tig	753.15	K	KDB
BasG	772.20	kJ/mol	NIST
ΔcH°liquid	-2644.00 ± 0.79	kJ/mol	NIST
ΔcH°solid	-2633.00	kJ/mol	NIST
μ	1.70	debye	KDB
LFL	2.35	% in Air	KDB
UFL	8.00	% in Air	KDB
Tflash,cc	289.26	K	KDB
Tflash,oc	284.26	K	KDB
ΔfG°	-178.80	kJ/mol	KDB
Rg	3.0190		KDB
ΔfH°gas	[-313.00; -309.70]	kJ/mol
ΔfH°gas	-312.80	kJ/mol	KDB
ΔfH°gas	-312.60 ± 0.88	kJ/mol	NIST
ΔfH°gas	-313.00 ± 1.50	kJ/mol	NIST
ΔfH°gas	-309.70	kJ/mol	NIST
ΔfH°liquid	[-359.30; -356.00]	kJ/mol
ΔfH°liquid	-359.20 ± 0.84	kJ/mol	NIST
ΔfH°liquid	-359.30 ± 0.79	kJ/mol	NIST
ΔfH°liquid	-356.00	kJ/mol	NIST
ΔfusH°	2.79	kJ/mol	Joback Calculated Property
ΔsubH°	41.00	kJ/mol	NIST
ΔvapH°	39.88	kJ/mol	Joback Calculated Property
IE	[9.90; 10.26]	eV
IE	9.90 ± 0.03	eV	NIST
IE	9.90 ± 0.03	eV	NIST
IE	9.97 ± 0.02	eV	NIST
IE	10.23	eV	NIST
IE	10.23	eV	NIST
IE	10.26	eV	NIST
IE	10.25 ± 0.03	eV	NIST
IE	10.25	eV	NIST
log10WS	-0.87		Crippen Calculated Property
logPoct/wat	0.777		Crippen Calculated Property
McVol	73.090	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
NFPA Health	1		KDB
Pc	[3970.00; 4232.00]	kPa
Pc	3972.00	kPa	KDB
Pc	3970.00 ± 20.00	kPa	NIST
Pc	3972.00	kPa	NIST
Pc	4232.00	kPa	NIST
ρc	[257.94; 270.02]	kg/m3
ρc	269.80 ± 1.48	kg/m3	NIST
ρc	270.02	kg/m3	NIST
ρc	257.94	kg/m3	NIST
Inp	[471.00; 543.00]
Inp	472.10		NIST
Inp	471.00		NIST
Inp	500.00		NIST
Inp	500.00		NIST
Inp	500.00		NIST
Inp	515.00		NIST
Inp	493.00		NIST
Inp	521.00		NIST
Inp	491.00		NIST
Inp	487.00		NIST
Inp	488.00		NIST
Inp	472.00		NIST
Inp	488.00		NIST
Inp	478.10		NIST
Inp	493.00		NIST
Inp	524.00		NIST
Inp	527.00		NIST
Inp	514.00		NIST
Inp	471.00		NIST
Inp	493.00		NIST
Inp	472.00		NIST
Inp	488.00		NIST
Inp	523.50		NIST
Inp	526.30		NIST
Inp	518.00		NIST
Inp	531.00		NIST
Inp	534.00		NIST
Inp	519.00		NIST
Inp	507.30		NIST
Inp	500.00		NIST
Inp	530.00		NIST
Inp	500.00		NIST
Inp	512.00		NIST
Inp	514.00		NIST
Inp	509.00		NIST
Inp	512.00		NIST
Inp	512.00		NIST
Inp	509.00		NIST
Inp	512.00		NIST
Inp	518.00		NIST
Inp	543.00		NIST
Inp	512.00		NIST
Inp	530.00		NIST
Inp	512.00		NIST
Inp	543.00		NIST
Inp	472.10		NIST
Inp	515.00		NIST
Inp	488.00		NIST
Inp	524.00		NIST
Inp	472.00		NIST
Inp	519.00		NIST
I	[863.00; 942.00]
I	930.00		NIST
I	942.00		NIST
I	930.00		NIST
I	942.00		NIST
I	934.00		NIST
I	897.00		NIST
I	867.00		NIST
I	906.00		NIST
I	881.00		NIST
I	863.00		NIST
I	882.00		NIST
I	902.00		NIST
I	891.00		NIST
I	879.00		NIST
I	914.00		NIST
I	875.00		NIST
I	900.00		NIST
I	880.00		NIST
I	871.00		NIST
I	897.00		NIST
I	920.00		NIST
I	871.00		NIST
I	916.00		NIST
I	934.00		NIST
I	875.00		NIST
I	897.00		NIST
I	875.00		NIST
S°liquid	[189.50; 197.50]	J/mol×K
S°liquid	189.50	J/mol×K	NIST
S°liquid	197.50	J/mol×K	NIST
S°solid,1 bar	170.87	J/mol×K	NIST
Tboil	[325.70; 375.50]	K
Tboil	355.50	K	KDB
Tboil	355.33	K	Isobari...
Tboil	355.55	K	Measure...
Tboil	355.80	K	Isobari...
Tboil	355.51	K	Isobari...
Tboil	355.59	K	Isobari...
Tboil	355.58	K	Vapor-L...
Tboil	355.56	K	Isobari...
Tboil	355.60 ± 0.30	K	NIST
Tboil	355.60 ± 0.30	K	NIST
Tboil	355.30 ± 0.40	K	NIST
Tboil	355.60 ± 0.30	K	NIST
Tboil	355.55 ± 0.30	K	NIST
Tboil	355.50	K	NIST
Tboil	355.00	K	NIST
Tboil	355.55 ± 0.25	K	NIST
Tboil	355.65 ± 0.25	K	NIST
Tboil	355.55 ± 0.30	K	NIST
Tboil	355.50	K	NIST
Tboil	355.35 ± 0.30	K	NIST
Tboil	355.70 ± 0.40	K	NIST
Tboil	355.45 ± 0.40	K	NIST
Tboil	355.40 ± 0.50	K	NIST
Tboil	355.70 ± 0.30	K	NIST
Tboil	355.70 ± 0.30	K	NIST
Tboil	355.60 ± 0.50	K	NIST
Tboil	355.65 ± 0.20	K	NIST
Tboil	355.47 ± 0.12	K	NIST
Tboil	355.47 ± 0.10	K	NIST
Tboil	354.61 ± 0.10	K	NIST
Tboil	355.95 ± 0.50	K	NIST
Tboil	355.70 ± 1.00	K	NIST
Tboil	355.55 ± 0.50	K	NIST
Tboil	355.50 ± 0.50	K	NIST
Tboil	355.40 ± 0.25	K	NIST
Tboil	353.65 ± 2.00	K	NIST
Tboil	355.65 ± 1.00	K	NIST
Tboil	355.65 ± 2.00	K	NIST
Tboil	354.65 ± 2.00	K	NIST
Tboil	355.95 ± 0.50	K	NIST
Tboil	355.15 ± 1.00	K	NIST
Tboil	355.95 ± 0.30	K	NIST
Tboil	355.75 ± 0.30	K	NIST
Tboil	354.65 ± 1.00	K	NIST
Tboil	355.15 ± 1.00	K	NIST
Tboil	355.25 ± 1.00	K	NIST
Tboil	355.15 ± 1.00	K	NIST
Tboil	355.75 ± 0.50	K	NIST
Tboil	355.56 ± 0.10	K	NIST
Tboil	355.60 ± 0.10	K	NIST
Tboil	355.60 ± 0.40	K	NIST
Tboil	Outlier 375.50 ± 0.30	K	NIST
Tboil	355.60 ± 0.10	K	NIST
Tboil	355.85 ± 0.50	K	NIST
Tboil	355.65 ± 1.00	K	NIST
Tboil	357.65 ± 2.00	K	NIST
Tboil	356.00 ± 1.00	K	NIST
Tboil	354.15 ± 3.00	K	NIST
Tboil	354.65 ± 1.00	K	NIST
Tboil	355.65 ± 2.00	K	NIST
Tboil	356.15 ± 1.00	K	NIST
Tboil	355.65 ± 0.10	K	NIST
Tboil	355.75 ± 0.50	K	NIST
Tboil	355.85 ± 0.50	K	NIST
Tboil	355.37 ± 0.20	K	NIST
Tboil	355.75 ± 0.30	K	NIST
Tboil	Outlier 325.70 ± 0.25	K	NIST
Tboil	355.70 ± 0.20	K	NIST
Tboil	355.75 ± 0.50	K	NIST
Tboil	356.01 ± 0.20	K	NIST
Tboil	355.15 ± 0.50	K	NIST
Tboil	355.40 ± 0.30	K	NIST
Tboil	355.10 ± 0.50	K	NIST
Tboil	355.72 ± 0.30	K	NIST
Tboil	356.20 ± 1.00	K	NIST
Tboil	356.09 ± 0.50	K	NIST
Tboil	354.90 ± 1.00	K	NIST
Tboil	355.55 ± 0.50	K	NIST
Tc	[506.20; 508.90]	K
Tc	506.20	K	KDB
Tc	506.35	K	Experim...
Tc	506.20 ± 0.30	K	NIST
Tc	506.20	K	NIST
Tc	506.20	K	NIST
Tc	508.90	K	NIST
Tc	508.10	K	NIST
Tfus	[297.99; 298.70]	K
Tfus	298.50	K	KDB
Tfus	298.70	K	Solid l...
Tfus	297.99	K	Solubil...
Ttriple	[298.50; 298.97]	K
Ttriple	298.96 ± 0.06	K	NIST
Ttriple	298.97 ± 0.06	K	NIST
Ttriple	298.50 ± 0.20	K	NIST
Vc	[0.275; 0.275]	m3/kmol
Vc	0.275	m3/kmol	KDB
Vc	0.275	m3/kmol	NIST
Zc	0.2595270		KDB
Zra	0.26		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[132.63; 187.30]	J/mol×K	[360.55; 591.55]
T(K) Ideal gas heat capacity (J/mol×K) 130 140 150 160 170 180 190 400 450 500 550
Cp,gas	133.40 ± 1.10	J/mol×K	360.55	NIST
Cp,gas	132.63	J/mol×K	365.15	NIST
Cp,gas	136.20 ± 1.10	J/mol×K	372.85	NIST
Cp,gas	137.95	J/mol×K	383.15	NIST
Cp,gas	139.20 ± 1.10	J/mol×K	385.65	NIST
Cp,gas	142.88	J/mol×K	401.15	NIST
Cp,gas	145.10 ± 1.10	J/mol×K	410.85	NIST
Cp,gas	148.07	J/mol×K	419.15	NIST
Cp,gas	153.55	J/mol×K	437.15	NIST
Cp,gas	151.90 ± 1.10	J/mol×K	439.85	NIST
Cp,gas	152.20 ± 1.10	J/mol×K	441.45	NIST
Cp,gas	159.10 ± 1.10	J/mol×K	470.75	NIST
Cp,gas	165.70 ± 1.10	J/mol×K	499.25	NIST
Cp,gas	172.60 ± 1.10	J/mol×K	528.75	NIST
Cp,gas	183.40 ± 1.10	J/mol×K	575.05	NIST
Cp,gas	187.30 ± 1.10	J/mol×K	591.55	NIST
Cp,liquid	[210.00; 224.90]	J/mol×K	[298.00; 300.00]
T(K) Liquid phase heat capacity (J/mol×K) 210 215 220 225 298 299 300
Cp,liquid	210.00	J/mol×K	298.00	NIST
Cp,liquid	215.37	J/mol×K	298.15	NIST
Cp,liquid	210.00	J/mol×K	298.15	NIST
Cp,liquid	224.90	J/mol×K	298.15	NIST
Cp,liquid	218.60	J/mol×K	298.15	NIST
Cp,liquid	221.88	J/mol×K	299.15	NIST
Cp,liquid	224.70	J/mol×K	300.00	NIST
Cp,solid	146.11	J/mol×K	298.15	NIST
η	[0.0007603; 0.0054860]	Pa×s	[293.15; 343.15]
T(K) Dynamic viscosity (Pa×s) 1.00e-3 2.00e-3 3.00e-3 4.00e-3 5.00e-3 300 320 340
η	0.0054860	Pa×s	293.15	Densiti...
η	0.0044330	Pa×s	298.15	Densiti...
η	0.0044360	Pa×s	298.15	Densiti...
η	0.0044330	Pa×s	298.15	Densiti...
η	0.0033550	Pa×s	303.15	Densiti...
η	0.0033550	Pa×s	303.15	Densiti...
η	0.0033780	Pa×s	303.15	Densiti...
η	0.0026110	Pa×s	308.15	Densiti...
η	0.0026110	Pa×s	308.15	Densiti...
η	0.0026905	Pa×s	308.15	Densiti...
η	0.0020740	Pa×s	313.15	Densiti...
η	0.0020740	Pa×s	313.15	Densiti...
η	0.0021423	Pa×s	313.15	Densiti...
η	0.0016850	Pa×s	318.15	Densiti...
η	0.0017369	Pa×s	318.15	Densiti...
η	0.0016850	Pa×s	318.15	Densiti...
η	0.0014284	Pa×s	323.15	Densiti...
η	0.0011964	Pa×s	328.15	Densiti...
η	0.0010160	Pa×s	333.15	Densiti...
η	0.0008734	Pa×s	338.15	Densiti...
η	0.0007603	Pa×s	343.15	Densiti...
ΔfusH	[0.49; 6.78]	kJ/mol	[286.10; 299.00]
T(K) Enthalpy of fusion at a given temperature (kJ/mol) 0 1 2 3 4 5 6 7 290 295
ΔfusH	0.83	kJ/mol	286.10	NIST
ΔfusH	0.49	kJ/mol	294.50	NIST
ΔfusH	6.78	kJ/mol	298.50	NIST
ΔfusH	6.70	kJ/mol	299.00	NIST
ΔfusH	6.70	kJ/mol	299.00	NIST
ΔsubH	51.30	kJ/mol	275.50	NIST
ΔvapH	[33.60; 46.50]	kJ/mol	[303.00; 479.50]
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 34 36 38 40 42 44 46 300 350 400 450
ΔvapH	46.20 ± 0.10	kJ/mol	303.00	NIST
ΔvapH	46.12 ± 0.05	kJ/mol	303.20	NIST
ΔvapH	44.90 ± 0.10	kJ/mol	313.00	NIST
ΔvapH	43.00 ± 0.10	kJ/mol	328.00	NIST
ΔvapH	44.70	kJ/mol	328.00	NIST
ΔvapH	42.50 ± 0.10	kJ/mol	330.00	NIST
ΔvapH	44.70	kJ/mol	331.50	NIST
ΔvapH	44.20	kJ/mol	334.00	NIST
ΔvapH	46.50	kJ/mol	334.50	NIST
ΔvapH	46.20	kJ/mol	337.00	NIST
ΔvapH	41.30 ± 0.10	kJ/mol	340.00	NIST
ΔvapH	43.40	kJ/mol	340.00	NIST
ΔvapH	41.00 ± 0.10	kJ/mol	343.00	NIST
ΔvapH	42.70	kJ/mol	345.50	NIST
ΔvapH	42.60	kJ/mol	346.00	NIST
ΔvapH	40.40 ± 0.10	kJ/mol	346.00	NIST
ΔvapH	42.10	kJ/mol	348.00	NIST
ΔvapH	40.00 ± 0.10	kJ/mol	349.00	NIST
ΔvapH	41.40	kJ/mol	355.00	NIST
ΔvapH	41.40	kJ/mol	355.00	NIST
ΔvapH	39.07	kJ/mol	355.50	NIST
ΔvapH	39.04	kJ/mol	355.90	KDB
ΔvapH	39.00 ± 0.10	kJ/mol	356.00	NIST
ΔvapH	37.20 ± 0.10	kJ/mol	368.00	NIST
ΔvapH	39.80	kJ/mol	409.00	NIST
ΔvapH	43.20	kJ/mol	418.00	NIST
ΔvapH	38.70	kJ/mol	439.50	NIST
ΔvapH	33.60	kJ/mol	479.50	NIST
ν	[0.0000027; 0.0000056]	m2/s	[298.15; 313.15]
ν	0.0000056	m2/s	298.15	Viscosi...
ν	0.0000027	m2/s	313.15	Viscosi...
Pvap	[8.96; 818.16]	kPa	[305.87; 423.15]
T(K) Vapor pressure (kPa) 0 100 200 300 400 500 600 700 800 350 400
Pvap	8.96	kPa	305.87	Vapor-L...
Pvap	11.51	kPa	310.08	Vapor-L...
Pvap	13.77	kPa	313.08	Vapour ...
Pvap	13.72	kPa	313.14	Vapor-L...
Pvap	16.11	kPa	316.04	Vapor-L...
Pvap	19.43	kPa	319.50	Vapor-L...
Pvap	23.07	kPa	322.78	Isother...
Pvap	23.28	kPa	322.94	Vapor-L...
Pvap	23.80	kPa	323.20	Vapor L...
Pvap	27.62	kPa	326.30	Vapor-L...
Pvap	32.74	kPa	329.74	Vapor-L...
Pvap	36.97	kPa	332.06	Vapor L...
Pvap	38.60	kPa	333.15	Isother...
Pvap	38.57	kPa	333.15	Vapor-L...
Pvap	40.00	kPa	333.90	Isobari...
Pvap	44.94	kPa	336.41	Vapor-L...
Pvap	52.29	kPa	339.74	Vapor-L...
Pvap	53.33	kPa	340.13	Isobari...
Pvap	60.80	kPa	343.15	Isother...
Pvap	61.09	kPa	343.25	Vapor-L...
Pvap	66.66	kPa	344.84	Isobari...
Pvap	66.66	kPa	345.21	Isobari...
Pvap	70.27	kPa	346.50	Vapor-L...
Pvap	79.99	kPa	349.23	Isobari...
Pvap	79.99	kPa	349.53	Isobari...
Pvap	80.85	kPa	349.84	Vapor-L...
Pvap	92.40	kPa	353.15	Isother...
Pvap	92.53	kPa	353.15	Vapor-L...
Pvap	93.32	kPa	353.32	Isobari...
Pvap	95.99	kPa	353.80	Isobari...
Pvap	98.66	kPa	354.61	Isobari...
Pvap	100.00	kPa	355.20	Isobari...
Pvap	100.91	kPa	355.31	Vapor-L...
Pvap	101.00	kPa	355.56	Isobari...
Pvap	101.33	kPa	355.59	Isobari...
Pvap	101.30	kPa	355.80	Isobari...
Pvap	142.60	kPa	364.50	Vapour ...
Pvap	142.60	kPa	364.50	Vapor L...
Pvap	143.30	kPa	364.52	Vapor L...
Pvap	143.00	kPa	364.52	Vapor-L...
Pvap	142.70	kPa	364.52	Isother...
Pvap	191.18	kPa	373.15	Vapor L...
Pvap	192.46	kPa	373.15	Vapor L...
Pvap	818.16	kPa	423.15	Vapor L...
Pvap	816.37	kPa	423.15	Vapor L...
n0	[1.37097; 1.38870]		[293.15; 323.15]
T(K) Refractive Index 1.37 1.38 1.38 1.39 1.39 300 310 320
n0	1.38810		293.15	Liquid-...
n0	1.38770		293.15	Isobari...
n0	1.38780		293.15	Isobari...
n0	1.38510		298.15	Isobari...
n0	1.38510		298.15	Volumet...
n0	1.38510		298.15	Excess ...
n0	1.38520		298.15	(Vapor ...
n0	1.38520		298.15	(Vapor ...
n0	1.38520		298.15	Excess ...
n0	1.38510		298.15	Isobari...
n0	1.38520		298.15	Excess ...
n0	1.38520		298.15	Activit...
n0	1.38481		298.15	Densiti...
n0	1.38500		298.15	Bubble-...
n0	1.38870		298.15	Bubble ...
n0	1.38520		298.15	Vapor-L...
n0	1.38220		303.15	Correla...
n0	1.38222		303.15	Experim...
n0	1.38222		303.15	Experim...
n0	1.38200		303.15	Isobari...
n0	1.37960		308.15	Densiti...
n0	1.37947		308.15	Experim...
n0	1.37947		308.15	Experim...
n0	1.37667		313.15	Experim...
n0	1.37667		313.15	Experim...
n0	1.37416		318.15	Densiti...
n0	1.37410		318.15	Excess ...
n0	1.37384		318.15	Experim...
n0	1.37384		318.15	Experim...
n0	1.37097		323.15	Experim...
n0	1.37097		323.15	Experim...
ρl	[725.06; 787.00]	kg/m3	[293.00; 348.15]
T(K) Liquid Density (kg/m3) 720 730 740 750 760 770 780 790 300 320 340
ρl	787.00	kg/m3	293.00	KDB
ρl	785.75	kg/m3	293.15	Densiti...
ρl	781.04	kg/m3	298.15	Vapor-l...
ρl	781.00	kg/m3	298.15	(Vapour...
ρl	780.78	kg/m3	298.15	Densiti...
ρl	780.44	kg/m3	298.15	Isother...
ρl	780.78	kg/m3	298.15	Surface...
ρl	780.63	kg/m3	298.15	Densiti...
ρl	781.20	kg/m3	298.15	Bubble ...
ρl	780.85	kg/m3	298.15	Excess ...
ρl	780.86	kg/m3	298.15	Liquid ...
ρl	780.72	kg/m3	298.15	Experim...
ρl	780.57	kg/m3	298.15	Measure...
ρl	780.61	kg/m3	298.15	Volumet...
ρl	779.48	kg/m3	299.15	Excess ...
ρl	779.48	kg/m3	299.15	Densiti...
ρl	775.46	kg/m3	303.15	Measure...
ρl	775.42	kg/m3	303.15	Volumet...
ρl	775.41	kg/m3	303.15	Influen...
ρl	775.51	kg/m3	303.15	Densiti...
ρl	775.10	kg/m3	303.15	Viscous...
ρl	775.38	kg/m3	303.15	Excess ...
ρl	775.39	kg/m3	303.15	Densiti...
ρl	770.25	kg/m3	308.15	Measure...
ρl	770.39	kg/m3	308.15	Densiti...
ρl	770.21	kg/m3	308.15	Experim...
ρl	770.19	kg/m3	308.15	Influen...
ρl	770.36	kg/m3	308.15	Densiti...
ρl	770.15	kg/m3	308.15	Densiti...
ρl	770.21	kg/m3	308.15	Volumet...
ρl	770.17	kg/m3	308.15	Excess ...
ρl	764.84	kg/m3	313.15	Densiti...
ρl	765.07	kg/m3	313.15	Densiti...
ρl	764.88	kg/m3	313.15	Influen...
ρl	765.26	kg/m3	313.15	Densiti...
ρl	764.92	kg/m3	313.15	Volumet...
ρl	764.95	kg/m3	313.15	Measure...
ρl	764.86	kg/m3	313.15	Excess ...
ρl	759.46	kg/m3	318.15	Densiti...
ρl	759.47	kg/m3	318.15	Excess ...
ρl	759.56	kg/m3	318.15	Measure...
ρl	760.13	kg/m3	318.15	Densiti...
ρl	759.49	kg/m3	318.15	Influen...
ρl	759.67	kg/m3	318.15	Densiti...
ρl	759.50	kg/m3	318.15	Experim...
ρl	759.42	kg/m3	318.15	Volumet...
ρl	753.94	kg/m3	323.15	Densiti...
ρl	753.95	kg/m3	323.15	Volumet...
ρl	754.10	kg/m3	323.15	Measure...
ρl	754.01	kg/m3	323.15	Excess ...
ρl	754.19	kg/m3	323.15	Densiti...
ρl	754.01	kg/m3	323.15	Influen...
ρl	748.62	kg/m3	328.15	Densiti...
ρl	742.70	kg/m3	333.15	Densiti...
ρl	742.95	kg/m3	333.15	Densiti...
ρl	737.19	kg/m3	338.15	Densiti...
ρl	731.31	kg/m3	343.15	Densiti...
ρl	725.06	kg/m3	348.15	Densiti...
ΔfusS	[1.66; 22.72]	J/mol×K	[286.10; 299.00]
ΔfusS	2.90	J/mol×K	286.10	NIST
ΔfusS	1.66	J/mol×K	294.50	NIST
ΔfusS	22.72	J/mol×K	298.50	NIST
ΔfusS	22.42	J/mol×K	299.00	NIST
csound,fluid	[1013.01; 1122.80]	m/s	[298.15; 323.15]
T(K) Speed of sound in fluid (m/s) 1020 1040 1060 1080 1100 1120 300 310 320
csound,fluid	1122.80	m/s	298.15	Densiti...
csound,fluid	1108.98	m/s	301.65	Influen...
csound,fluid	1099.02	m/s	303.15	Influen...
csound,fluid	1098.21	m/s	303.15	Tempera...
csound,fluid	1101.90	m/s	303.15	Excess ...
csound,fluid	1088.33	m/s	305.65	Influen...
csound,fluid	1077.71	m/s	308.15	Influen...
csound,fluid	1067.22	m/s	310.65	Influen...
csound,fluid	1056.40	m/s	313.15	Excess ...
csound,fluid	1055.36	m/s	313.15	Tempera...
csound,fluid	1056.73	m/s	313.15	Influen...
csound,fluid	1057.40	m/s	313.15	Densiti...
csound,fluid	1046.12	m/s	315.65	Influen...
csound,fluid	1035.66	m/s	318.15	Influen...
csound,fluid	1025.17	m/s	320.65	Influen...
csound,fluid	1014.76	m/s	323.15	Influen...
csound,fluid	1013.01	m/s	323.15	Tempera...
csound,fluid	1015.90	m/s	323.15	Excess ...
γ	[0.02; 0.02]	N/m	[298.15; 328.15]
T(K) Surface Tension (N/m) 0.02 0.02 0.02 0.02 0.02 0.02 300 310 320
γ	0.02	N/m	298.15	Equilib...
γ	0.02	N/m	308.15	Equilib...
γ	0.02	N/m	318.15	Equilib...
γ	0.02	N/m	318.20	KDB
γ	0.02	N/m	328.15	Equilib...

Datasets

1. Viscosity, Pa*s (1)
2. Mass density, kg/m3 (3)

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
303.15	101.33	0.0034
Reference

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
308.15	101.30	770.14
323.15	101.30	753.94
323.15	10000.00	764.58
323.15	25000.00	778.73
323.15	50000.00	798.2
323.15	75000.00	813.79
323.15	100000.00	827.34
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
308.15	97.00	770.2
348.15	98.00	725.1
303.15	99.00	775.3
313.15	99.00	764.8
323.15	99.00	753.9
343.15	99.00	731.0
353.15	99.00	719.0
318.15	100.00	759.4
338.15	100.00	737.1
328.15	101.00	748.4
333.15	103.00	742.8
358.15	103.00	712.8
358.15	293.00	713.1
348.15	295.00	725.3
313.15	298.00	765.0
318.15	298.00	759.6
323.15	298.00	754.1
328.15	298.00	748.7
303.15	298.00	775.5
308.15	298.00	770.4
363.15	299.00	706.4
353.15	300.00	719.3
343.15	305.00	731.3
333.15	307.00	743.1
338.15	309.00	737.3
318.15	498.00	759.8
348.15	498.00	725.7
358.15	498.00	713.4
328.15	499.00	748.9
303.15	499.00	775.7
308.15	500.00	770.6
353.15	501.00	719.6
313.15	502.00	765.2
323.15	502.00	754.4
333.15	502.00	743.3
363.15	502.00	706.8
343.15	503.00	731.6
338.15	505.00	737.6
308.15	897.00	771.0
353.15	897.00	720.2
328.15	898.00	749.4
338.15	898.00	738.1
348.15	898.00	726.2
303.15	898.00	776.1
358.15	899.00	714.0
318.15	901.00	760.3
323.15	901.00	754.9
343.15	901.00	732.1
363.15	901.00	707.4
313.15	904.00	765.7
333.15	915.00	743.8
353.15	1000.00	720.3
303.15	1002.00	776.2
308.15	1002.00	771.1
343.15	1002.00	732.2
363.15	1002.00	707.6
338.15	1003.00	738.2
358.15	1003.00	714.2
323.15	1004.00	755.0
348.15	1004.00	726.4
328.15	1005.00	749.5
318.15	1006.00	760.4
333.15	1007.00	744.0
313.15	1009.00	765.8
343.15	2000.00	733.6
353.15	2000.00	721.8
328.15	2001.00	750.7
338.15	2001.00	739.5
318.15	2001.00	761.5
363.15	2001.00	709.2
323.15	2003.00	756.1
348.15	2006.00	727.8
303.15	2007.00	777.1
358.15	2008.00	715.7
308.15	2009.00	772.1
333.15	2013.00	745.2
313.15	2016.00	766.8
353.15	2999.00	723.2
308.15	3000.00	773.1
328.15	3001.00	751.9
343.15	3001.00	734.9
348.15	3001.00	729.2
323.15	3002.00	757.2
318.15	3003.00	762.6
358.15	3003.00	717.3
338.15	3005.00	740.8
363.15	3005.00	710.8
333.15	3006.00	746.4
313.15	3006.00	767.8
303.15	3007.00	778.1
303.15	4999.00	780.0
353.15	4999.00	726.1
328.15	5001.00	754.1
318.15	5002.00	764.7
333.15	5002.00	748.8
363.15	5002.00	713.9
338.15	5003.00	743.2
358.15	5003.00	720.2
323.15	5004.00	759.4
343.15	5005.00	737.5
348.15	5005.00	731.9
308.15	5006.00	775.1
313.15	5010.00	769.9
348.15	6999.00	734.5
353.15	6999.00	728.8
328.15	7001.00	756.3
323.15	7002.00	761.5
303.15	7003.00	781.9
358.15	7003.00	723.0
343.15	7004.00	740.0
333.15	7005.00	751.1
318.15	7005.00	766.7
308.16	7005.00	777.0
313.15	7006.00	771.8
338.15	7014.00	745.6
363.15	7023.00	716.9
303.15	8992.00	783.7
353.15	8998.00	731.4
318.15	8999.00	768.7
333.15	9001.00	753.3
358.15	9001.00	725.8
363.15	9001.00	719.7
323.15	9002.00	763.5
328.15	9004.00	758.5
338.15	9004.00	747.9
313.15	9005.00	773.7
308.15	9006.00	778.8
348.15	9012.00	737.0
343.15	9033.00	742.4
358.15	9998.00	727.1
328.15	9999.00	759.5
333.15	9999.00	754.3
338.15	10002.00	749.0
323.15	10002.00	764.5
318.15	10002.00	769.7
353.15	10003.00	732.6
303.15	10005.00	784.6
313.15	10007.00	774.7
308.15	10007.00	779.7
363.15	10009.00	721.1
348.15	10014.00	738.2
343.15	10020.00	743.6
353.15	11997.00	735.1
338.15	11998.00	751.2
328.15	11999.00	761.6
318.15	11999.00	771.6
303.15	11999.00	786.3
323.15	12000.00	766.5
343.15	12001.00	745.8
333.15	12003.00	756.5
348.15	12003.00	740.6
308.15	12005.00	781.5
313.15	12005.00	776.5
358.15	12010.00	729.7
363.15	12038.00	723.8
363.15	14998.00	727.6
338.15	14999.00	754.4
348.15	14999.00	744.0
323.15	14999.00	769.3
358.15	14999.00	733.3
333.15	15000.00	759.6
353.15	15001.00	738.7
343.15	15002.00	749.1
328.15	15004.00	764.5
313.15	15005.00	779.2
318.15	15010.00	774.4
308.15	15021.00	784.1
333.15	17995.00	762.5
338.15	17997.00	757.5
318.15	17998.00	777.0
323.15	17998.00	772.1
348.15	17999.00	747.3
353.15	17999.00	742.1
363.15	18000.00	731.3
343.15	18001.00	752.3
313.15	18003.00	781.8
328.15	18006.00	767.4
308.16	18006.00	786.6
358.15	18040.00	736.9
328.15	19995.00	769.2
333.15	19997.00	764.4
358.15	19997.00	739.1
308.15	19998.00	788.2
323.15	20000.00	773.9
348.15	20000.00	749.4
353.15	20000.00	744.2
318.15	20006.00	778.8
338.15	20007.00	759.4
313.15	20015.00	783.5
343.15	20018.00	754.4
363.15	20033.00	733.7
343.15	21994.00	756.4
358.15	21995.00	741.3
333.15	21996.00	766.2
348.15	21998.00	751.5
338.15	21999.00	761.4
318.15	21999.00	780.5
353.15	21999.00	746.4
328.15	22000.00	771.0
323.15	22000.00	775.7
313.15	22002.00	785.1
308.15	22003.00	789.8
363.15	22005.00	735.9
308.15	24990.00	792.2
318.15	24994.00	782.9
333.15	24994.00	768.9
328.15	24996.00	773.6
348.15	24996.00	754.4
353.15	24997.00	749.4
338.15	25000.00	764.2
323.15	25000.00	778.2
363.15	25000.00	739.2
313.15	25007.00	787.5
358.15	25017.00	744.5
343.15	25026.00	759.3
343.15	27993.00	762.1
333.15	27993.00	771.6
338.15	27994.00	766.9
358.15	27994.00	747.6
323.15	27995.00	780.7
348.15	27995.00	757.3
328.15	27998.00	776.2
353.15	27999.00	752.5
313.15	28002.00	789.9
318.15	28005.00	785.4
308.15	28006.00	794.5
363.15	28009.00	742.4
358.15	29991.00	749.6
313.15	30000.00	791.4
318.15	30001.00	787.0
323.15	30002.00	782.4
333.15	30003.00	773.3
343.15	30004.00	763.9
353.15	30004.00	754.4
328.15	30005.00	777.9
308.15	30005.00	796.0
338.15	30011.00	768.6
363.15	30011.00	744.4
348.15	30045.00	759.3
343.15	32000.00	765.7
348.15	32000.00	761.0
323.15	32000.00	784.0
318.15	32001.00	788.5
313.16	32001.00	792.9
358.15	32001.00	751.5
353.15	32003.00	756.3
333.15	32004.00	775.0
328.15	32005.00	779.5
338.15	32005.00	770.4
363.15	32033.00	746.5
333.15	32850.00	775.7
333.15	32871.00	775.7
348.15	32878.00	761.8
343.15	32963.00	766.6
363.15	32982.00	747.4
353.15	32985.00	757.1
318.15	32993.00	789.3
358.15	32997.00	752.5
338.15	32998.00	771.2
323.15	33000.00	784.7
343.15	33001.00	766.6
313.15	33001.00	793.7
323.15	33001.00	784.7
353.15	33002.00	757.2
318.15	33002.00	789.3
348.15	33012.00	761.9
313.15	33012.00	793.6
363.15	33012.00	747.4
358.15	33015.00	752.5
328.15	33023.00	780.3
338.15	33033.00	771.2
328.15	33038.00	780.4
333.15	34000.00	776.6
348.15	34000.00	762.8
353.15	34000.00	758.1
323.15	34000.00	785.5
343.15	34002.00	767.5
313.15	34006.00	794.4
338.15	34007.00	772.0
318.15	34010.00	790.0
328.15	34013.00	781.1
363.15	34035.00	748.4
358.15	34056.00	753.5
333.15	34990.00	777.4
363.15	34999.00	749.3
338.15	35000.00	772.9
348.15	35001.00	763.7
318.15	35001.00	790.8
343.15	35003.00	768.3
353.15	35004.00	759.0
328.15	35004.00	781.9
323.15	35004.00	786.2
313.15	35008.00	795.1
358.15	35075.00	754.4
358.15	37998.00	757.0
363.15	37998.00	752.1
318.15	38000.00	793.0
323.15	38000.00	788.5
348.15	38001.00	766.3
328.15	38002.00	784.3
333.15	38004.00	779.8
313.15	38012.00	797.2
343.15	38027.00	770.8
338.15	38031.00	775.3
363.16	38458.00	752.5
353.15	38477.00	762.2
363.15	39147.00	753.2
333.15	39997.00	781.4
343.15	39998.00	772.5
323.15	39998.00	790.0
348.15	39999.00	768.0
358.15	40001.00	758.8
313.15	40002.00	798.6
353.15	40002.00	763.4
363.15	40009.00	753.9
318.15	40010.00	794.4
338.15	40024.00	776.9
328.15	40024.00	785.8
348.15	41997.00	769.6
323.15	41998.00	791.5
338.15	41998.00	778.5
333.15	41998.00	782.9
363.15	41998.00	755.7
328.15	41999.00	787.2
343.15	42000.00	774.1
358.15	42007.00	760.6
313.15	42007.00	800.0
318.15	42021.00	795.9
353.15	42035.00	765.1
338.15	43195.00	779.4
338.15	44574.00	780.4
333.15	44909.00	785.1
313.15	44997.00	802.0
348.15	44999.00	772.0
363.15	44999.00	758.4
323.15	45000.00	793.6
358.15	45002.00	763.1
328.15	45002.00	789.4
318.15	45005.00	797.9
353.15	45022.00	767.6
338.15	46152.00	781.6
358.15	47995.00	765.5
323.15	47996.00	795.7
363.15	47996.00	760.9
328.15	47997.00	791.6
318.15	47997.00	799.9
353.15	48092.00	770.1
333.15	48119.00	787.4
338.15	48333.00	783.3
353.15	49989.00	771.5
328.15	49992.00	793.0
318.15	49998.00	801.3
363.15	49998.00	762.5
333.15	50000.00	788.7
323.15	50000.00	797.1
358.15	50001.00	767.0
338.15	50050.00	784.5
328.16	51996.00	794.3
323.15	51998.00	798.4
363.15	52002.00	764.2
318.15	52004.00	802.6
333.15	52050.00	790.2
338.15	52462.00	786.3
328.15	55000.00	796.4
318.15	55002.00	804.6
363.15	55003.00	766.6
323.15	55006.00	800.5
333.15	55010.00	792.3
338.15	56690.00	789.2
318.15	57994.00	806.5
323.15	57995.00	802.4
328.15	57995.00	798.3
333.15	57996.00	794.3
363.15	57998.00	768.9
363.15	59999.00	770.4
323.15	60000.00	803.7
318.15	60002.00	807.7
328.15	60003.00	799.6
333.15	60003.00	795.6
338.15	60003.00	791.5
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	5.61	780.885
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.65]	kPa	[278.50; 374.62]	The Yaw...
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.44210e+01
Coefficient B			-2.46322e+03
Coefficient C			-1.04219e+02
Temperature range, min.			278.50
Temperature range, max.			374.62
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350
Pvap	1.33	kPa	278.50	Calculated Property
Pvap	3.01	kPa	289.18	Calculated Property
Pvap	6.24	kPa	299.86	Calculated Property
Pvap	11.97	kPa	310.54	Calculated Property
Pvap	21.54	kPa	321.22	Calculated Property
Pvap	36.68	kPa	331.90	Calculated Property
Pvap	59.56	kPa	342.58	Calculated Property
Pvap	92.77	kPa	353.26	Calculated Property
Pvap	139.33	kPa	363.94	Calculated Property
Pvap	202.65	kPa	374.62	Calculated Property
Pvap	[4.06; 4016.87]	kPa	[293.00; 506.20]	KDB Vap...
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			9.13446e+01
Coefficient B			-8.70216e+03
Coefficient C			-1.06233e+01
Coefficient D			1.15210e-06
Temperature range, min.			293.00
Temperature range, max.			506.20
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 4000 300 400 500
Pvap	4.06	kPa	293.00	Calculated Property
Pvap	16.67	kPa	316.69	Calculated Property
Pvap	53.39	kPa	340.38	Calculated Property
Pvap	140.56	kPa	364.07	Calculated Property
Pvap	316.31	kPa	387.76	Calculated Property
Pvap	626.86	kPa	411.44	Calculated Property
Pvap	1119.44	kPa	435.13	Calculated Property
Pvap	1834.21	kPa	458.82	Calculated Property
Pvap	2797.34	kPa	482.51	Calculated Property
Pvap	4016.87	kPa	506.20	Calculated Property

Similar Compounds

Find more compounds similar to 2-Propanol, 2-methyl-.

Mixtures

• 2-Propanol, 2-methyl- + Aniline
• 2-Propanol, 2-methyl- + Propane, 2-methoxy-2-methyl-
• 2-Propanol, 2-methyl- + Acetic acid, 1,1-dimethylethyl ester
• 2-Propanol, 2-methyl- + Isobutane
• 2-Propanol, 2-methyl- + Phenol, 3-chloro-
• 2-Propanol, 2-methyl- + Phenol, 4-chloro-
• 2-Propanol, 2-methyl- + Phenol, 3-chloro- + Phenol, 4-chloro-
• 2-Propanol, 2-methyl- + 1,3-Dioxolane + Water
• 2-Propanol, 2-methyl- + Phenol, 2-methyl-
• 2-Propanol, 2-methyl- + p-Cresol
• 2-Propanol, 2-methyl- + Formamide, N,N-dimethyl-
• 2-Propanol, 2-methyl- + 2-Pyrrolidinone, 1-methyl-
• 2-Propanol, 2-methyl- + Butane
• 2-Propanol, 2-methyl- + Ethanol + Cyclohexane, methyl-
• 2-Propanol, 2-methyl- + Benzene, chloro-
• 2-Propanol, 2-methyl- + 1,4-Dioxane
• 2-Propanol, 2-methyl- + Heptane
• 2-Propanol, 2-methyl- + Octane
• 2-Propanol, 2-methyl- + Nonane
• 2-Propanol, 2-methyl- + Decane

Find more mixtures with 2-Propanol, 2-methyl-.

Sources

• KDB Pure (Korean Thermophysical Properties Databank)
• KDB Vapor Pressure Data
• Crippen Method
• Crippen Method
• Densities and Volumetric Properties of Binary Mixtures of Aniline with 1-Propanol, 2-Propanol, 2-Methyl-1-Propanol, and 2-Methyl-2-Propanol at Temperatures from 293.15 to 318.15 K
• Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
• Isobaric vapor-liquid equilibria for the binary systems isobutyl alcohol + isobutyl acetate and tert-butyl alcohol + tert-butyl acetate at 20 and 101.3 kPa
• Vapour liquid equilibrium for the 2-methylpropane + methanol, +ethanol, +2-propanol, +2-butanol and +2-methyl-2-propanol systems at 313.15K
• Isobaric vapor liquid phase equilibria for the binary systems of tert-butanol + 2-ethyl-1-hexanol and n-butanol + 2-ethyl-1-hexanol
• Solid liquid equilibria of mixtures containing tert-butanol, m-chlorophenol, and p-chlorophenol and development of adductive crystallization processes
• Viscous synergy and antagonism and isentropic compressibility of ternary mixtures containing 1,3-dioxolane, water and monoalkanols at 303.15K
• Activity coefficients of the binary mixtures of a-cresol or p-cresol with C l-C4 aliphatic alcohols near ambient pressure
• Excess Gibbs energies of selected binary mixtures formed by N,N-dimethyl formamide at 95.5 kPa
• Excess volumes and excess enthalpies of N-methyl-2-pyrrolidone with branched alcohols
• Vapour liquid equilibrium for the systems butane + methanol, +2-propanol, +1-butanol, +2-butanol, +2-methyl-2-propanol at 364.5K
• Isobaric vapor liquid equilibrium for ternary mixtures of ethanol and methylcyclohexane with 3-methylpentane and tert-butyl alcohol at 101.3 kPa
• Influence of chain length and degree of branching of alcohol + chlorobenzene mixtures on determination and modelling of VE by CEOS and CEOS/GE mixing rules
• Measurement and correlation of binary vapor liquid equilibria of isomeric butanols with 1,4-dioxane
• Solubilities of cinnamic acid esters in binary mixtures of ionic liquids and organic solvents
• Viscosity of the binary systems 2-methyl-2-propanol with n-alkanes at T = (303.15, 308.15, 313.15, 318.15 and 323.15) K: Prediction and correlation - New UNIFAC-VISCO interaction parameters
• Experimental study of the isochoric heat capacity of tert-butanol in the critical and supercritical regions
• Thermodynamic study of aqueous two phase systems for some aliphatic alcohols + sodium thiosulfate + water
• Liquid liquid equilibrium of 1-propanol, 2-propanol, 2-methyl-2-propanol or 2-butanol + sodium sulfite + water aqueous two phase systems
• Solubility of chlocyphos in different solvents
• The study of phase behavior of aqueous 1-propanol/2-propanol/2-butanol/2-methyl-2-propanol systems in the presence of disodium tartrate or disodium succinate at T = 298.15 K
• Volumetric behavior of carbon dioxide + 2-methyl-1-propanol and carbondioxide + 2-methyl-2-propanol mixtures at 313.15 K
• The effect of temperature on the liquid-liquid equilibria of somealiphatic alcohols + di-sodium hydrogen citrate + water systems: Experimental and correlation
• Vapor-liquid equilibria of binary systems composed of polyoxyethylene 4-octylphenyl ether and alcohols: Experimental measurements and correlation
• Liquid-liquid equilibria of 1-octyl-3-methylimidazolium hexafluorophosphate with 1-propanol or tert-butanol in the critical region
• Measurement and modeling of volumetric properties and speeds of sound of several mixtures of alcohol liquids containing 1-propanol and 2-propanol at T= (298.15 - 323.15) K and ambient pressure
• Liquid-liquid equilibrium for the ternary system water + 2-methyl-1-propanol + butyl acetate and water + 2-methyl-2-propanol + butyl acetate at (298.15 and 323.15) K
• Mesoscale solubilization and critical phenomena in binary and quasi-binary solutions of hydrotropes
• Solubility of diazepam in water + tert-butyl alcohol solvent mixtures: Part 1. Experimental data and thermodynamic analysis
• 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
• Excess specific volume of water + tert-butyl alcohol solvent mixtures: Experimental data, modeling and derived excess partial specific thermodynamic quantities.
• Evaluation of the solvent structural effect upon the vapor-liquid equilibrium of [C4C1im][Cl] + Alcohols
• High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
• Solubility and dissolution characteristics of capecitabine in pure lower alcohols and water with methanol mixture solvents at atmospheric pressure and different temperatures
• Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
• Measurement and correlation of aqueous biphasic systems composed of alcohol (1-propanol/ 2-propanol/tert-butanol) + (NH4)2SO4 + H2O at 298 K and a textile dye partition.
• 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
• Isobaric vapor-liquid equilibria for tert-butanol + water with single and mixed ionic liquids as solvents at 101.3 kPa
• (Vapour + liquid) equilibrium of binary mixtures (1,3-dioxolane or 1,4-dioxane + 2-methyl-1-propanol or 2-methyl-2-propanol) at isobaric conditions
• (Liquid + liquid) phase behavior for systems containing (aromatic + TBA + methylcyclohexane)
• Henry's constants and infinite dilution activity coefficients of propane, propene, butane, isobutane, 1-butene, isobutene, trans-2-butene, and 1,3-butadiene in isobutanol and tert-butanol
• Densities and speeds of sound for binary mixtures of (1,3-dioxolane or 1,4-dioxane) with (2-methyl-1-propanol or 2-methyl-2-propanol) at the temperatures 298.15 K and 313.15 K
• Salt effect on (liquid + liquid) equilibrium of (water + tertbutanol + 1-butanol) system: Experimental data and correlation
• (Vapor + liquid) equilibria of binary mixtures formed by iso-octane with a variety of compounds at 95.8 kPa
• Excess molar enthalpies of dimethyl carbonate and (butanol isomers and 1-pentanol) at T = (298.15, 313.15, and 328.15) K and p = (0.1, 1.0, and 10.0) MPa
• Henry's law constants and infinite dilution activity coefficients of cis-2-butene, dimethylether, chloroethane, and 1,1-difluoroethane in methanol, 1-propanol, 2-propanol, 1-butanol, 2-butanol, isobutanol, tert-butanol, 1-pentanol, 2-pentanol, 3-pentanol, 2-methyl-1-butanol, 3-methyl-1-butanol, and 2-methyl-2-butanol
• Bubble point temperatures of the binary mixtures of nitrobenzene with C1 C4 aliphatic alcohols at 94.95 kPa
• Adiabatic compressibility of pseudo-binary aqueous solutions of tert-butyl alcohol and dimethylsulfoxide as a result of ultrasonic investigations
• (Vapor + liquid) equilibria of the binary mixtures of m-cresol with C1 C4 aliphatic alcohols at 95.5 kPa
• Excess Gibbs free energies of the binary mixtures of acetonitrile with butanols at 94.83 kPa
• Temperature influence on mixing properties of {ethyl tert-butyl ether (ETBE) + gasoline additives}
• Solubility and Stability of Nesquehonite (MgCO3 *3H2O) in NaCl, KCl, MgCl2, and NH4Cl Solutions
• Isobaric (vapour + liquid) equilibrium for N-methyl-2-pyrrolidone with branched alcohols
• (Liquid + liquid) equilibrium of {water + phenol + (1-butanol, or 2-butanol, or tert-butanol)} systems
• Densities and volume properties of (water + tert-butanol) over the temperature range of (274.15 to 348.15) K at pressure of 0.1 MPa
• Experimental and predicted refractive index properties in ternary mixtures of associated liquids
• The buffering-out effect and phase separation in aqueous solutions of EPPS buffer with 1-propanol, 2-propanol, or 2-methyl-2-propanol at T = 298.15 K
• Solubilities of some organic solutes in 1-ethyl-3-methylimidazolium acetate. Chromatographic measurements and predictions from COSMO-RS
• 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
• Determination and correlation of the solubility for diosgenin in alcohols solvents
• 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
• Thermodynamic investigation of the ATPSs composed of some (aliphatic alcohol + sodium carbonate + water) ternary systems
• 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
• Liquid phase PVTx properties of (water + tert-butanol) binary mixtures at temperatures from 278.15 to 323.15 K and pressures from 0.1 to 100 MPa. I. Experimental results, excess and partial molar volumes
• 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
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-hydroxyethyl)- 3-methylimidazolium trifluorotris(perfluoroethyl)phosphate
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tricyanomethanide
• Thermodynamics and activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylmorpholinium tricyanomethanide
• Measurement of activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-hexyl-1,4-diaza[2.2.2]bicyclooctanium bis(trifluoromethylsulfonyl)imide using gas-liquid chromatography
• Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
• Equilibrium surface tension and the interaction energy of DMSO with tert-butyl alcohol or iso-amyl alcohol at various temperatures
• 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, physicochemical and thermodynamic properties for organic solutes and water in the ionic liquid ethyl-dimethyl-(2-methoxyethyl)ammonium trifluorotris-(perfluoroethyl)phosphate
• A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
• Isobaric vapour-liquid equilibrium of (tert-butanol + water) system with biological buffer TRIS at 101.3 kPa
• 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
• 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
• Experimental and modeling vapor-liquid equilibrium for the binary systems {ethanol(1) + glycerol(2)} and {tert-butanol(1) + glycerol(2)} at high pressures
• The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
• Volumetric properties of monoethanolamine and alcohol binary mixtures at different temperatures and 0.1 MPa
• Isobaric vapor-liquid equilibria for the extractive distillation of tert-butyl alcohol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
• Experimental Determination and Modeling of Densities and Refractive Indices of the Binary Systems Alcohol + Dicyclohexylamine at T = (288.15 to 323.15) K
• Experimental and theoretical excess molar properties of imidazolium based ionic liquids with isomers of butanol
• Measurement and Correlation of the Solubility of Antioxidant 626 in Alcohols
• Measurements of Infinite Dilution Activity Coefficients of Alkanols in the Ionic Liquid Tributylmethylammonium Methyl Sulfate Using HS-SPME/GC/FID
• P-rho-T Data for 2-Butanol and tert-Butanol from (283.15 to 363.15) K and (303.15 to 363.15) at pressures up to 66 MPa
• Isobaric Phase Equilibrium of tert-Butyl Alcohol + Glycerol at Local and Subatmospheric Pressures, Volumetric Properties, and Molar Refractivity from 303.15 to 333.15 K of tert-Butyl Alcohol + Glycerol, tert-Butyl Alcohol + Water, and Water + Glycerol Binary Systems
• 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
• Isobaric Vapor Liquid Equilibrium for the Binary Systems of sec-Butyl Acetate + n-Butyl Alcohol, Isobutyl Alcohol, or tert-Butyl Alcohol at 101.3 kPa
• Determination of Ternary Liquid Liquid Equilibria for Dimethyl Carbonate + 2-Methyl-1-propanol or 2-Methyl-2-propanol + Water Systems at T = 303.15 and 313.15 K
• Phase Separation of Alcohol (1-Propanol, 2-Propanol, or tert-Butanol) from Its Aqueous Solution in the Presence of Biological Buffer MOPS
• Isobaric Vapor-Liquid Equilibrium for Binary and Ternary Systems of tert-Butanol + tert-Butyl Acetate + Chlorobenzene at 101.33 kPa
• Equilibrium Diagrams of Water + NaCl or KCl + 2-Methyl 2-Propanol at the Boiling Temperature and 101.3 kPa
• Isobaric Vapor-Liquid Equilibria and Excess Quantities for Binary Mixtures of an Ethyl Ester + tert-Butanol and a New Approach to VLE Data Processing
• High-Pressure Vapor-Liquid Equilibria for CO2 + 2-Butanol, CO2 + iso-Butanol and CO2 + tert-Butanol Systems
• Solubility of Benzimidazoles in Alcohols
• Bubble Temperatures of the Binary Mixtures of Dimethylcarbonate with Some Alcohols at 95.8 kPa
• Bubble-Temperature Measurements on Some Binary Mixtures Formed by Tetrahydrofuran or Amyl Alcohol with Hydrocarbons, Chlorohydrocarbons, or Butanols at (94.6 or 95.8) kPa
• Viscosities of Binary Mixtures of Isomeric Butanols or Isomeric Chlorobutanes with 2-Methyltetrahydrofuran
• Isothermal Vapor-Liquid Equilibria for Binary Mixtures Composed of the Closely Boiling Compounds 1,2-Dimethoxybenzene and 2-Methoxyphenol with an Adducted Agent: tert-Butanol or Morpholine
• Thermodynamic Functions for Transfer of Anthracene from Water to (Water + Alcohol) Mixtures at 298.15K
• Vapor Liquid Equilibrium for the Trans-2-Butene + Methanol, + Ethanol, + 2-Propanol, + 2-Butanol and + 2-Methyl-2-Propanol Systems at 332 K
• Isothermal Vapor Liquid Equilibrium for Binary 2-Methylpropene - C1-C4 Alcohol-Systems
• Excess Properties and Isobaric Vapor-Liquid Equilibria for Binary Mixtures of Methyl Esters + tert-Butanol
• Densities and Viscosities of Binary Mixtures of 1-Chlorobutane with Butanol Isomers at Several Temperatures
• Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
• Excess Molar Volumes and Surface Tensions of 1,2,4-Trimethylbenzene and 1,3,5-Trimethylbenzene with 1-Butanol, 2-Methyl-1-propanol, 2-Butanol, and 2-Methyl-2-propanol at 298.15 K
• Solubility of Cesium Nitrate in Alcohol Aqueous Solutions at (25, 35 and 45 ) C
• Phase Diagrams of Some Aliphatic Alcohols + Potassium or Sodium Citrate + Water at 25 deg C
• Densities and Viscosities of Binary Mixtures of 1-Bromobutane with Butanol Isomers at Several Temperatures
• Densities, Viscosities, and Refractive Indices for Binary and Ternary Mixtures of Ethanol, 2-Methylpropan-2-ol, and 2,2,4-Trimethylpentane
• Experimental and Predicted Results of Anomeric Equilibrium of Glucose in Alcohols
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 8. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography
• Isothermal Vapor Liquid Equilibrium for 2-Methylpropene + Methanol, + 1-Propanol, + 2-Propanol, + 2-Butanol, and + 2-Methyl-2-propanol Binary Systems at 364.5 K
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 9. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in Trimethyl-butylammonium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography and Static Method
• Temperature Effect on the Liquid-Liquid Equilibria for Some Aliphatic Alcohols + Water + K2CO3 Systems
• Correlation and Prediction of Excess Quantities and Vapor-Liquid Equilibria of Alkyl Esters + tert-Butyl Alcohol: Experimental Data for Propyl Esters + tert-Butyl Alcohol
• Experimental Study of Thermodynamic Properties of Mixtures Containing Ionic Liquid 1-Ethyl-3-methylimidazolium Ethyl Sulfate Using Gas-Liquid Chromatography and Transpiration Method
• Vapor-Liquid Equilibrium for Benzaldehyde with 1-Methylethylbenzene and for 2-Methyl-propan-2-ol with 2,4,4-Trimethyl-1-pentene
• Surface Tensions of the Ternary Mixtures Containing an Isomeric Butanol + n-Hexane + 1-Chlorobutane at 298.15 K
• Experimental Determination of Densities and Refractive Indices of the Ternary Mixture 2-Methyl-2-propanol + Cyclohexylamine + n-Heptane at T = (303.15 to 323.15) K
• Isobaric Vapor Liquid Equilibrium Data for the Binary Mixtures 2-Methyl Propan-2-ol with Tetraethoxysilane and 1-Phenyl Ethanone at 95.5 kPa
• Binodal Curves and Tie-Lines of Aliphatic Alcohols + Diammonium Hydrogen Citrate + Water Ternary Systems: Measurement and Modeling
• Liquid Liquid Equilibrium of Some Aliphatic Alcohols + Disodium Tartrate + Water Aqueous Two-Phase Systems at 298.15 K
• Isobaric Vapor Liquid Equilibrium Data of 2-Methyl-propan-2-ol (1) + Heptan-1-ol (2), Methanol (1) + Heptan-1-ol (2), Ethanol (1) + Heptan-1-ol (2), and Propan-1-ol (1) + Heptan-1-ol (2) at 96.5 kPa
• Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
• Liquid Liquid Equilibrium for the Ternary System 2-Methyl-2-propanol + 1-Pentanol + Water at T = (303.15, 328.15, and 353.15) K
• Experimental Vapor Liquid Equilibria for the Systems {2-Ethyl-1-hexanol + Glycerol + CO2} and {2-Methyl-2-propanol + Glycerol + CO2}
• Densities and Viscosities of Binary Mixtures of 2-Butanol + Isobutanol, 2-Butanol + tert-Butanol, and Isobutanol + tert-Butanol from (308.15 to 343.15) K
• Vapor Liquid Equilibrium for Several Compounds Relevant to the Biofuels Industry Modeled with the Wilson Equation
• Isobaric Vapor Liquid Equilibrium of tert-Butyl Alcohol + Water + Triethanolamine-Based Ionic Liquid Ternary Systems at 101.3 kPa
• Temperature Dependence of Limiting Activity Coefficients, Henry s Law Constants, and Related Infinite Dilution Properties of Branched (C3 and C4) Alkanols in Water. Measurement, Critical Compilation, Correlation, and Recommended Data
• Vapor-Liquid Equilibrium and Excess Gibbs Energies of Hexane + N,N-Dimethyl Formamide, 2-Methylpropan-2-ol + 2-Aminophenol, N,N-Dimethyl Formamide, and 2-Propanol + Diisopropyl Amine at 94.4 kPa
• Excess Enthalpy, Density, and Speed of Sound for the Mixtures a-Pinene + 2-Methyl-1-propanol or 2-Methyl-2-propanol at Several Temperatures
• Vapor Liquid Equilibrium for Butane + Methanol, + Ethanol, + 2-Propanol, + 2-Butanol, and + 2-Methyl-2-Propanol (TBA) at 323 K
• Liquid Liquid Equilibria for the Ternary System Water + Methyl Isobutyl Ketone + tert-Butyl Alcohol at Several Temperatures
• Vapor Liquid Equilibrium for the Systems trans-2-Butene + Methanol, + 1-Propanol, + 2-Propanol, + 2-Butanol, and + 2-Methyl-2-propanol at 364.5 K
• Vapor Liquid Equilibrium for the Systems 2-Methylpropane + Methanol, + 2-Propanol, + 2-Butanol, and + 2-Methyl-2-propanol at 364.5 K
• Densities and Viscosities of the Ternary Mixtures 2-Methyl-1-propanol (or 2-Methyl-2-propanol) + N-Hexane + 1-Chlorobutane at 298.15 K
• Vapor-Liquid Equilibrium for the cis-2-Butene + Methanol, + 2-Propanol, + 2-Butanol, + 2-Methyl-2-propanol Systems at 364.5 K
• Isobaric Vapor-Liquid Equilibria for Tetrahydropyran and Alcohol Systems
• Vapor-Liquid Equilibrium for 1-Butene + Methanol, + 1-Propanol, + 2-Propanol, + 2-Butanol, and 2-Methyl-2-propanol (TBA) at 364.5 K
• Activity Coefficients at Infinite Dilution of Alkanols in the Ionic Liquids 1-Butyl-3-methylimidazolium Hexafluorophosphate, 1-Butyl-3-methylimidazolium Methyl Sulfate, and 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Amide Using the Dilutor Technique
• Liquid-Liquid Equilibria in Ternary Systems 2-Methylbutane + 2-Methyl-2-propanol + Water and Pentane + 2-Methyl-2-propanol + Water at 293.15 K
• Viscosity of Water + tert-Butyl Alcohol (2-Methyl-2-propanol) Mixtures at Low Temperatures and High Pressure
• Unusual S-Shaped Binodal Curves of the System Water + Lithium Chloride + 2-Methyl-2-propanol
• Densities, Viscosities, and Excess Molar Enthalpies of 2-Pyrrolidone + Butanol Isomers at T ) (293.15, 298.15, and 303.15) K
• Isothermal Vapor-Liquid Equilibrium of Ternary Mixtures Containing 2-Methyl-1-propanol or 2-Methyl-2-propanol, n-Hexane, and 1-Chlorobutane at 298.15 K
• Solubilities of Cinnamic Acid Esters in Organic Solvents
• Densities and Viscosities of Binary Mixtures of n-Butanol with 2-Butanol, Isobutanol, and tert-Butanol from (303.15 to 343.15) K
• Liquid-Liquid Equilibria for Aliphatic Alcohols + Dipotassium Oxalate + Water
• 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
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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Outlier This icon means that the value is more than 2 standard deviations away from the property mean.