Chemical Properties of Butane, 2-chloro- (CAS 78-86-4)

InChI

InChI=1S/C4H9Cl/c1-3-4(2)5/h4H,3H2,1-2H3

InChI Key

BSPCSKHALVHRSR-UHFFFAOYSA-N

Formula

C4H9Cl

SMILES

CCC(C)Cl

Molecular Weight¹

92.57

CAS

78-86-4

Other Names

• 1-METHYLPROPYL CHLORIDE
• 2-CHLOROBUTANE
• SEC-BUTYL CHLORIDE
• UN 1127
• sec-C4H9Cl

• ω : Acentric Factor.
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_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_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• V_c : Critical Volume (m³/kmol).
• Z_c : Critical Compressibility.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.3000		KDB
ΔcH°liquid	-2685.47 ± 0.95	kJ/mol	NIST
μ	2.10	debye	KDB
ΔfG°	-53.51	kJ/mol	KDB
ΔfH°gas	[-166.66; -161.60]	kJ/mol
ΔfH°gas	-161.60	kJ/mol	KDB
ΔfH°gas	-166.66 ± 0.99	kJ/mol	NIST
ΔfH°liquid	-198.43 ± 0.99	kJ/mol	NIST
ΔfusH°	6.79	kJ/mol	Joback Calculated Property
ΔvapH°	[28.98; 31.77]	kJ/mol
ΔvapH°	31.68	kJ/mol	NIST
ΔvapH°	31.77 ± 0.08	kJ/mol	NIST
ΔvapH°	31.53	kJ/mol	NIST
ΔvapH°	31.50 ± 0.10	kJ/mol	NIST
ΔvapH°	31.60 ± 0.10	kJ/mol	NIST
ΔvapH°	31.56 ± 0.06	kJ/mol	NIST
ΔvapH°	Outlier 28.98 ± 0.06	kJ/mol	NIST
IE	[10.50; 10.72]	eV
IE	10.57 ± 0.06	eV	NIST
IE	10.59	eV	NIST
IE	10.53	eV	NIST
IE	10.50 ± 0.10	eV	NIST
IE	10.65 ± 0.03	eV	NIST
IE	10.72	eV	NIST
log10WS	[-1.96; -1.96]
log10WS	-1.96		Aq. Solubility Prediction
log10WS	-1.96		Estimated Solubility
logPoct/wat	2.024		Crippen Calculated Property
McVol	79.460	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
NFPA Health	2		KDB
Pc	3950.00	kPa	KDB
Inp	[582.00; 616.00]
Inp	589.00		NIST
Inp	582.00		NIST
Inp	586.00		NIST
Inp	588.00		NIST
Inp	591.00		NIST
Inp	609.00		NIST
Inp	599.00		NIST
Inp	598.38		NIST
Inp	598.87		NIST
Inp	598.00		NIST
Inp	611.00		NIST
Inp	Outlier 616.00		NIST
Inp	601.00		NIST
Inp	601.00		NIST
Inp	601.00		NIST
Inp	601.00		NIST
Inp	598.38		NIST
Tboil	[340.85; 342.20]	K
Tboil	341.40	K	KDB
Tboil	341.26	K	Study of tetrahydropyran-chlorobutane VLE using the a o and o o approaches
Tboil	341.23	K	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Tboil	341.26	K	Vapor-Liquid Equilibrium and Volumetric Measurements for Binary Mixtures of 1,4-Dioxane with Isomeric Chlorobutanes
Tboil	Outlier 342.20	K	NIST
Tboil	341.40	K	NIST
Tboil	340.85 ± 0.60	K	NIST
Tboil	341.15 ± 1.50	K	NIST
Tboil	341.00 ± 3.00	K	NIST
Tboil	340.90 ± 3.00	K	NIST
Tboil	341.40 ± 0.20	K	NIST
Tboil	341.40 ± 0.30	K	NIST
Tc	[520.60; 520.60]	K
Tc	520.60	K	KDB
Tc	520.60	K	NIST
Tfus	[137.58; 141.85]	K
Tfus	141.80	K	KDB
Tfus	137.58	K	Aq. Solubility Prediction
Tfus	141.85 ± 0.50	K	NIST
Vc	0.305	m3/kmol	KDB
Zc	0.2783270		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[118.70; 160.95]	J/mol×K	[327.91; 504.53]
Cp,gas	118.70	J/mol×K	327.91	Joback Calculated Property
Cp,gas	126.45	J/mol×K	357.35	Joback Calculated Property
Cp,gas	133.91	J/mol×K	386.78	Joback Calculated Property
Cp,gas	141.08	J/mol×K	416.22	Joback Calculated Property
Cp,gas	147.98	J/mol×K	445.66	Joback Calculated Property
Cp,gas	154.60	J/mol×K	475.09	Joback Calculated Property
Cp,gas	160.95	J/mol×K	504.53	Joback Calculated Property
Cp,liquid	[160.90; 174.00]	J/mol×K	[298.15; 298.15]
Cp,liquid	160.90	J/mol×K	298.15	NIST
Cp,liquid	174.00	J/mol×K	298.15	NIST
η	[0.0003371; 0.0004631]	Pa×s	[283.15; 313.15]
η	0.0004631	Pa×s	283.15	Viscosities of Binary Mixtures Containing Isomeric Chlorobutanes and Diisopropylether: Experimental and Predicted Values
η	0.0004631	Pa×s	283.15	Experimental and Predicted Viscosities of Binary Mixtures Containing Chlorinated and Oxygenated Compounds
η	0.0004365	Pa×s	288.15	Viscosities of Binary Mixtures Containing Isomeric Chlorobutanes and Diisopropylether: Experimental and Predicted Values
η	0.0004365	Pa×s	288.15	Experimental and Predicted Viscosities of Binary Mixtures Containing Chlorinated and Oxygenated Compounds
η	0.0004167	Pa×s	293.15	Experimental and Predicted Viscosities of Binary Mixtures Containing Chlorinated and Oxygenated Compounds
η	0.0004167	Pa×s	293.15	Viscosities of Binary Mixtures Containing Isomeric Chlorobutanes and Diisopropylether: Experimental and Predicted Values
η	0.0003993	Pa×s	298.15	Viscosities of Binary Mixtures Containing Isomeric Chlorobutanes and Diisopropylether: Experimental and Predicted Values
η	0.0003938	Pa×s	298.15	Densities and Viscosities of the Binary Mixtures of Tetrahydrofuran with Isomeric Chlorobutanes at 298.15 K and 313.15 K
η	0.0003993	Pa×s	298.15	Experimental and Predicted Viscosities of Binary Mixtures Containing Chlorinated and Oxygenated Compounds
η	0.0003800	Pa×s	303.15	Viscosities of Binary Mixtures Containing Isomeric Chlorobutanes and Diisopropylether: Experimental and Predicted Values
η	0.0003800	Pa×s	303.15	Experimental and Predicted Viscosities of Binary Mixtures Containing Chlorinated and Oxygenated Compounds
η	0.0003615	Pa×s	308.15	Experimental and Predicted Viscosities of Binary Mixtures Containing Chlorinated and Oxygenated Compounds
η	0.0003615	Pa×s	308.15	Viscosities of Binary Mixtures Containing Isomeric Chlorobutanes and Diisopropylether: Experimental and Predicted Values
η	0.0003443	Pa×s	313.15	Viscosities of Binary Mixtures Containing Isomeric Chlorobutanes and Diisopropylether: Experimental and Predicted Values
η	0.0003443	Pa×s	313.15	Experimental and Predicted Viscosities of Binary Mixtures Containing Chlorinated and Oxygenated Compounds
η	0.0003371	Pa×s	313.15	Densities and Viscosities of the Binary Mixtures of Tetrahydrofuran with Isomeric Chlorobutanes at 298.15 K and 313.15 K
ΔvapH	[28.20; 33.10]	kJ/mol	[292.50; 358.00]
ΔvapH	31.80	kJ/mol	292.50	NIST
ΔvapH	30.70 ± 0.10	kJ/mol	313.00	NIST
ΔvapH	33.10	kJ/mol	321.50	NIST
ΔvapH	30.90	kJ/mol	328.00	NIST
ΔvapH	29.90 ± 0.10	kJ/mol	328.00	NIST
ΔvapH	29.20	kJ/mol	341.20	KDB
ΔvapH	29.17	kJ/mol	341.40	NIST
ΔvapH	29.10 ± 0.10	kJ/mol	343.00	NIST
ΔvapH	28.20 ± 0.10	kJ/mol	358.00	NIST
ν	[0.0000004; 0.0000005]	m2/s	[283.15; 313.15]
ν	0.0000005	m2/s	283.15	Experimental and Predicted Kinematic Viscosities for Alkane + Chloroalkane Mixtures
ν	0.0000005	m2/s	298.15	Thermophysical Properties of Mixtures of Tetrahydropyran with Chlorobutanes
ν	0.0000005	m2/s	298.15	Viscosities of Binary Mixtures of Isomeric Butanols or Isomeric Chlorobutanes with 2-Methyltetrahydrofuran
ν	0.0000005	m2/s	298.15	Experimental and Predicted Kinematic Viscosities for Alkane + Chloroalkane Mixtures
ν	0.0000004	m2/s	313.15	Thermophysical Properties of Mixtures of Tetrahydropyran with Chlorobutanes
ν	0.0000004	m2/s	313.15	Viscosities of Binary Mixtures of Isomeric Butanols or Isomeric Chlorobutanes with 2-Methyltetrahydrofuran
ν	0.0000004	m2/s	313.15	Experimental and Predicted Kinematic Viscosities for Alkane + Chloroalkane Mixtures
Pvap	[13.36; 102.78]	kPa	[288.15; 341.75]
Pvap	13.36	kPa	288.15	Experimental and predicted vapour-liquid equilibrium of the binary mixtures n-heptane + chlorobutane isomers
Pvap	13.36	kPa	288.15	Isothermal vapour-liquid equilibria and excess enthalpies for the binary mixtures containing an isomeric chlorobutane and diisopropyl ether
Pvap	13.36	kPa	288.15	Experimental and predicted properties of the binary mixtures containing an isomeric chlorobutane and butyl ethyl ether
Pvap	13.36	kPa	288.15	Article Previous Article Next Article Articles ASAP Phase Equilibrium of Binary Mixtures of n-Hexane + Branched Chlorobutanes: Experimental Results and Group Contribution Predictions
Pvap	20.91	kPa	298.15	Article Previous Article Next Article Articles ASAP Phase Equilibrium of Binary Mixtures of n-Hexane + Branched Chlorobutanes: Experimental Results and Group Contribution Predictions
Pvap	20.91	kPa	298.15	Experimental and predicted vapour-liquid equilibrium of the binary mixtures n-heptane + chlorobutane isomers
Pvap	20.91	kPa	298.15	Isothermal vapour-liquid equilibria and excess enthalpies for the binary mixtures containing an isomeric chlorobutane and diisopropyl ether
Pvap	20.91	kPa	298.15	Experimental and predicted properties of the binary mixtures containing an isomeric chlorobutane and butyl ethyl ether
Pvap	31.55	kPa	308.15	Experimental and predicted properties of the binary mixtures containing an isomeric chlorobutane and butyl ethyl ether
Pvap	31.55	kPa	308.15	Article Previous Article Next Article Articles ASAP Phase Equilibrium of Binary Mixtures of n-Hexane + Branched Chlorobutanes: Experimental Results and Group Contribution Predictions
Pvap	31.55	kPa	308.15	Experimental and predicted vapour-liquid equilibrium of the binary mixtures n-heptane + chlorobutane isomers
Pvap	31.55	kPa	308.15	Isothermal vapour-liquid equilibria and excess enthalpies for the binary mixtures containing an isomeric chlorobutane and diisopropyl ether
Pvap	48.34	kPa	319.80	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	50.22	kPa	320.75	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	53.30	kPa	322.42	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	59.07	kPa	325.25	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	61.30	kPa	326.25	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	65.21	kPa	328.15	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	74.49	kPa	331.90	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	78.06	kPa	333.25	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	80.00	kPa	334.01	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	83.29	kPa	335.20	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	89.61	kPa	337.34	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	93.45	kPa	338.75	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	96.38	kPa	339.65	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	101.30	kPa	341.23	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	102.78	kPa	341.75	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
n0	[1.38562; 1.40226]		[283.15; 313.15]
n0	1.40226		283.15	Volumetric, Acoustic, and Refractive Properties of Isomeric Chlorobutanes with Diisopropyl Ether
n0	1.39953		288.15	Volumetric, Acoustic, and Refractive Properties of Isomeric Chlorobutanes with Diisopropyl Ether
n0	1.39680		293.15	Volumetric, Acoustic, and Refractive Properties of Isomeric Chlorobutanes with Diisopropyl Ether
n0	1.39404		298.15	Volumetric and refractive properties of binary mixtures containing 1,4-dioxane and chloroalkanes
n0	1.39404		298.15	Volumetric, Acoustic, and Refractive Properties of Isomeric Chlorobutanes with Diisopropyl Ether
n0	1.39125		303.15	Volumetric, Acoustic, and Refractive Properties of Isomeric Chlorobutanes with Diisopropyl Ether
n0	1.38844		308.15	Volumetric, Acoustic, and Refractive Properties of Isomeric Chlorobutanes with Diisopropyl Ether
n0	1.38573		313.15	Volumetric and refractive properties of binary mixtures containing 1,4-dioxane and chloroalkanes
n0	1.38562		313.15	Volumetric, Acoustic, and Refractive Properties of Isomeric Chlorobutanes with Diisopropyl Ether
ρl	[867.37; 873.00]	kg/m3	[293.00; 298.15]
ρl	873.00	kg/m3	293.00	KDB
ρl	867.37	kg/m3	298.15	Surface Tension of Mixtures of Tetrahydrofuran or Tetrahydropyran with Isomeric Chlorobutanes
ρl	867.37	kg/m3	298.15	Surface study of mixtures containing cyclic ethers and isomeric chlorobutanes
ρl	867.37	kg/m3	298.15	Thermodynamic study of 2-methyl-tetrahydrofuran with isomeric chlorobutanes
γ	0.02	N/m	293.20	KDB

Datasets

Mass density, kg/m3

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
100.00	283.15	884.17
100.00	288.15	878.94
100.00	293.15	872.99
100.00	298.15	867.31
100.00	303.15	861.63
100.00	308.15	856.25
100.00	313.15	850.12
100.00	318.15	844.59
100.00	323.15	838.39
100.00	328.15	832.81
2000.00	283.15	886.22
2000.00	288.15	881.0
2000.00	293.15	875.11
2000.00	298.15	869.59
2000.00	303.15	863.89
2000.00	308.15	858.73
2000.00	313.15	852.55
2000.00	318.15	847.15
2000.00	323.15	841.07
2000.00	328.15	835.59
5000.00	283.15	889.26
5000.00	288.15	884.23
5000.00	293.15	878.43
5000.00	298.15	872.97
5000.00	303.15	867.45
5000.00	308.15	862.31
5000.00	313.15	856.44
5000.00	318.15	850.8
5000.00	323.15	845.19
5000.00	328.15	839.88
7000.00	283.15	891.28
7000.00	288.15	886.25
7000.00	293.15	880.56
7000.00	298.15	875.17
7000.00	303.15	869.74
7000.00	308.15	864.71
7000.00	313.15	858.81
7000.00	318.15	853.7
7000.00	323.15	847.87
7000.00	328.15	842.66
10000.00	283.15	894.16
10000.00	288.15	889.3
10000.00	293.15	883.72
10000.00	298.15	878.41
10000.00	303.15	873.12
10000.00	308.15	868.08
10000.00	313.15	862.43
10000.00	318.15	857.33
10000.00	323.15	851.64
10000.00	328.15	846.54
20000.00	283.15	903.34
20000.00	288.15	898.71
20000.00	293.15	893.43
20000.00	298.15	888.39
20000.00	303.15	883.39
20000.00	308.15	878.72
20000.00	313.15	873.34
20000.00	318.15	868.68
20000.00	323.15	863.29
20000.00	328.15	858.56
30000.00	283.15	911.71
30000.00	288.15	907.27
30000.00	293.15	902.22
30000.00	298.15	897.49
30000.00	303.15	892.74
30000.00	308.15	888.3
30000.00	313.15	883.24
30000.00	318.15	878.85
30000.00	323.15	873.67
30000.00	328.15	869.22
40000.00	283.15	919.47
40000.00	288.15	915.2
40000.00	293.15	910.33
40000.00	298.15	905.79
40000.00	303.15	901.25
40000.00	308.15	897.03
40000.00	313.15	892.21
40000.00	318.15	887.93
40000.00	323.15	883.17
40000.00	328.15	878.94
50000.00	283.15	926.7
50000.00	288.15	922.6
50000.00	293.15	917.87
50000.00	298.15	913.53
50000.00	303.15	909.12
50000.00	308.15	905.05
50000.00	313.15	900.48
50000.00	318.15	896.41
50000.00	323.15	891.75
50000.00	328.15	887.7
60000.00	283.15	933.46
60000.00	288.15	929.48
60000.00	293.15	924.95
60000.00	298.15	920.75
60000.00	303.15	916.44
60000.00	308.15	912.57
60000.00	313.15	908.09
60000.00	318.15	904.23
60000.00	323.15	899.75
60000.00	328.15	895.82
65000.00	283.15	936.67
65000.00	288.15	932.78
65000.00	293.15	928.34
65000.00	298.15	924.15
65000.00	303.15	919.96
65000.00	308.15	916.04
65000.00	313.15	911.73
65000.00	318.15	907.86
65000.00	323.15	903.54
65000.00	328.15	899.7
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.65]	kPa	[246.42; 364.63]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.46808e+01
Coefficient B			-3.17313e+03
Coefficient C			-2.59560e+01
Temperature range, min.			246.42
Temperature range, max.			364.63
Pvap	1.33	kPa	246.42	Calculated Property
Pvap	3.00	kPa	259.55	Calculated Property
Pvap	6.17	kPa	272.69	Calculated Property
Pvap	11.82	kPa	285.82	Calculated Property
Pvap	21.28	kPa	298.96	Calculated Property
Pvap	36.28	kPa	312.09	Calculated Property
Pvap	59.02	kPa	325.23	Calculated Property
Pvap	92.17	kPa	338.36	Calculated Property
Pvap	138.86	kPa	351.50	Calculated Property
Pvap	202.65	kPa	364.63	Calculated Property
Pvap	[3.14e-06; 3884.52]	kPa	[141.85; 520.60]	KDB Vapor Pressure Data
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			5.80053e+01
Coefficient B			-5.45019e+03
Coefficient C			-6.53399e+00
Coefficient D			5.89810e-06
Temperature range, min.			141.85
Temperature range, max.			520.60
Pvap	3.14e-06	kPa	141.85	Calculated Property
Pvap	4.09e-03	kPa	183.93	Calculated Property
Pvap	0.29	kPa	226.02	Calculated Property
Pvap	4.79	kPa	268.10	Calculated Property
Pvap	33.63	kPa	310.18	Calculated Property
Pvap	140.83	kPa	352.27	Calculated Property
Pvap	422.67	kPa	394.35	Calculated Property
Pvap	1015.30	kPa	436.43	Calculated Property
Pvap	2093.96	kPa	478.52	Calculated Property
Pvap	3884.52	kPa	520.60	Calculated Property

Similar Compounds

Find more compounds similar to Butane, 2-chloro-.

Mixtures

• Tetrahydropyran + Butane, 2-chloro-
• Butane, 2-chloro- + Tetrahydrofuran
• Diisopropyl ether + Butane, 2-chloro-
• Butane, 1-ethoxy- + Butane, 2-chloro-
• Propane, 2-methoxy-2-methyl- + Butane, 2-chloro-
• Heptane + Butane, 2-chloro-
• Butane, 2-chloro- + Cyclohexane
• Toluene + Butane, 2-chloro-
• Butane, 2-chloro- + 1,4-Dioxane
• 1,3-Dioxolane + Butane, 2-chloro-
• n-Hexane + Butane, 2-chloro-
• Butane, 2-chloro- + Furan, tetrahydro-2-methyl-
• Butane, 2-chloro- + Pentane, 3-methyl-
• Butane, 2-chloro- + Butane, 2,2-dimethyl-
• 1-Propanol, 2-methyl- + Butane, 2-chloro-
• Acetic acid, butyl ester + Butane, 2-chloro-
• Acetic acid, butyl ester + 1-Propanol, 2-methyl- + Butane, 2-chloro-
• Benzene + Butane, 2-chloro-
• o-Xylene + Butane, 2-chloro-
• p-Xylene + Butane, 2-chloro-

Find more mixtures with Butane, 2-chloro-.

Sources

• KDB Pure (Korean Thermophysical Properties Databank)
• KDB Vapor Pressure Data
• Cheméo Relay (1.0)
• Crippen Method
• Thermophysical Properties of Mixtures of Tetrahydropyran with Chlorobutanes
• Surface Tension of Mixtures of Tetrahydrofuran or Tetrahydropyran with Isomeric Chlorobutanes
• Viscosities of Binary Mixtures Containing Isomeric Chlorobutanes and Diisopropylether: Experimental and Predicted Values
• Experimental and Predicted Viscosities of Binary Mixtures Containing Chlorinated and Oxygenated Compounds
• Study of tetrahydropyran-chlorobutane VLE using the a o and o o approaches
• Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
• Isothermal vapour-liquid equilibria and excess enthalpies for the binary mixtures containing an isomeric chlorobutane and diisopropyl ether
• Experimental and predicted vapour-liquid equilibrium of the binary mixtures n-heptane + chlorobutane isomers
• Volumetric and refractive properties of binary mixtures containing 1,4-dioxane and chloroalkanes
• Surface study of mixtures containing cyclic ethers and isomeric chlorobutanes
• Volumetric and acoustic behaviour of systems containing n-hexane, or n-heptane and isomeric chlorobutanes
• Application of ERAS-model and Prigogine-Flory-Patterson theory to excess molar volumes for ternary mixtures of (2-chlorobutane + butylacetate + isobutanol) at T = 298.15 K
• Experimental and predicted properties of the binary mixtures containing an isomeric chlorobutane and butyl ethyl ether
• Thermodynamic study of 2-methyl-tetrahydrofuran with isomeric chlorobutanes
• Excess properties from p.rho.T data for n-heptane + isomeric chlorobutane mixtures
• Vapor-Liquid Equilibrium and Volumetric Measurements for Binary Mixtures of 1,4-Dioxane with Isomeric Chlorobutanes
• Viscosities of Binary Mixtures of Isomeric Butanols or Isomeric Chlorobutanes with 2-Methyltetrahydrofuran
• Densities and Viscosities of the Binary Mixtures of Tetrahydrofuran with Isomeric Chlorobutanes at 298.15 K and 313.15 K
• Volumetric, Acoustic, and Refractive Properties of Isomeric Chlorobutanes with Diisopropyl Ether
• Experimental and Predicted Kinematic Viscosities for Alkane + Chloroalkane Mixtures
• Volumetric Properties of Short-Chain Chloroalkanes
• Article Previous Article Next Article Articles ASAP Phase Equilibrium of Binary Mixtures of n-Hexane + Branched Chlorobutanes: Experimental Results and Group Contribution Predictions
• Molar Excess Volume of sec- and tert-Butyl Chloride with Aromatic Hydrocarbons at T = 298.15 K
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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