Chemical Properties of Butane, 1-chloro- (CAS 109-69-3)

InChI

InChI=1S/C4H9Cl/c1-2-3-4-5/h2-4H2,1H3

InChI Key

VFWCMGCRMGJXDK-UHFFFAOYSA-N

Formula

C4H9Cl

SMILES

CCCCCl

Molecular Weight¹

92.57

CAS

109-69-3

Other Names

• 1-chlorobutane
• Chlorure de butyle
• NBC wormer
• NCI-C06155
• NSC 8419
• Sure Shot
• butyl chloride
• n-C4H9Cl
• n-Propylcarbinyl chloride
• n-butyl chloride

• 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.
• I : Polar retention indices.
• 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).
• 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.

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	0.2180		KDB
ΔcH°liquid	[-2704.10; -2695.80]	kJ/mol
ΔcH°liquid	-2695.80 ± 1.10	kJ/mol	NIST
ΔcH°liquid	-2704.10 ± 8.40	kJ/mol	NIST
μ	2.00	debye	KDB
ΔfG°	-38.81	kJ/mol	KDB
ΔfH°gas	[-154.60; -147.40]	kJ/mol
ΔfH°gas	-147.40	kJ/mol	KDB
ΔfH°gas	-154.60 ± 1.20	kJ/mol	NIST
ΔfH°liquid	-188.20 ± 1.20	kJ/mol	NIST
ΔfusH°	10.31	kJ/mol	Joback Calculated Property
ΔvapH°	[33.50; 33.63]	kJ/mol
ΔvapH°	Outlier 33.63	kJ/mol	NIST
ΔvapH°	33.50	kJ/mol	NIST
ΔvapH°	33.52	kJ/mol	NIST
ΔvapH°	33.50 ± 0.10	kJ/mol	NIST
ΔvapH°	33.50 ± 0.10	kJ/mol	NIST
ΔvapH°	33.52 ± 0.06	kJ/mol	NIST
IE	[10.46; 10.94]	eV
IE	10.64 ± 0.19	eV	NIST
IE	10.63	eV	NIST
IE	10.46 ± 0.05	eV	NIST
IE	10.94	eV	NIST
IE	10.50 ± 0.07	eV	NIST
IE	10.67 ± 0.03	eV	NIST
IE	10.84	eV	NIST
log10WS	[-2.03; -2.03]
log10WS	-2.03		Aq. Solubility Prediction
log10WS	-2.03		Estimated Solubility
logPoct/wat	2.025		Crippen Calculated Property
McVol	79.460	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
NFPA Health	2		KDB
Pc	3680.00	kPa	KDB
Inp	[607.00; 659.61]
Inp	646.10		NIST
Inp	641.60		NIST
Inp	647.30		NIST
Inp	642.50		NIST
Inp	639.60		NIST
Inp	639.00		NIST
Inp	638.30		NIST
Inp	Outlier 659.61		NIST
Inp	639.00		NIST
Inp	639.50		NIST
Inp	640.00		NIST
Inp	630.40		NIST
Inp	654.00		NIST
Inp	641.00		NIST
Inp	631.00		NIST
Inp	648.00		NIST
Inp	644.00		NIST
Inp	641.00		NIST
Inp	641.00		NIST
Inp	653.00		NIST
Inp	644.00		NIST
Inp	646.00		NIST
Inp	648.00		NIST
Inp	641.00		NIST
Inp	Outlier 607.00		NIST
Inp	Outlier 612.00		NIST
Inp	638.00		NIST
Inp	637.00		NIST
Inp	637.00		NIST
Inp	637.00		NIST
Inp	637.00		NIST
Inp	641.00		NIST
Inp	637.00		NIST
Inp	641.00		NIST
Inp	642.00		NIST
Inp	635.00		NIST
Inp	642.00		NIST
Inp	648.30		NIST
Inp	639.10		NIST
Inp	631.00		NIST
Inp	637.00		NIST
Inp	648.30		NIST
Inp	638.00		NIST
I	[832.00; 858.00]
I	832.00		NIST
I	842.00		NIST
I	858.00		NIST
Tboil	[323.95; 381.40]	K
Tboil	351.52	K	Study of tetrahydropyran-chlorobutane VLE using the a o and o o approaches
Tboil	351.53	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	351.52	K	Vapor-Liquid Equilibrium and Volumetric Measurements for Binary Mixtures of 1,4-Dioxane with Isomeric Chlorobutanes
Tboil	351.60	K	KDB
Tboil	351.60	K	NIST
Tboil	Outlier 381.40 ± 0.20	K	NIST
Tboil	351.70	K	NIST
Tboil	351.55	K	NIST
Tboil	351.65 ± 0.50	K	NIST
Tboil	351.35 ± 0.50	K	NIST
Tboil	350.65 ± 1.50	K	NIST
Tboil	351.55 ± 0.30	K	NIST
Tboil	351.59 ± 0.07	K	NIST
Tboil	Outlier 323.95 ± 0.60	K	NIST
Tboil	350.85 ± 0.40	K	NIST
Tboil	351.65 ± 0.20	K	NIST
Tboil	350.60 ± 0.30	K	NIST
Tboil	351.20 ± 0.50	K	NIST
Tboil	351.75 ± 0.30	K	NIST
Tc	[542.00; 542.00]	K
Tc	542.00	K	KDB
Tc	542.00	K	NIST
Tfus	[149.95; 150.12]	K
Tfus	150.10	K	KDB
Tfus	150.12	K	Aq. Solubility Prediction
Tfus	150.05	K	NIST
Tfus	149.95 ± 0.05	K	NIST
Tfus	150.05 ± 0.20	K	NIST
Vc	0.312	m3/kmol	KDB
Zc	0.2547810		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[156.22; 173.09]	J/mol×K	[284.15; 353.15]
Cp,liquid	156.22	J/mol×K	284.15	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	156.75	J/mol×K	286.65	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	157.28	J/mol×K	289.15	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	157.70	J/mol×K	291.65	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	158.27	J/mol×K	294.15	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	158.86	J/mol×K	296.65	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	159.53	J/mol×K	298.15	NIST
Cp,liquid	158.90	J/mol×K	298.15	NIST
Cp,liquid	159.64	J/mol×K	298.15	NIST
Cp,liquid	159.48	J/mol×K	299.15	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	160.05	J/mol×K	301.65	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	160.50	J/mol×K	304.15	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	161.06	J/mol×K	306.65	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	161.59	J/mol×K	309.15	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	162.24	J/mol×K	311.65	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	162.92	J/mol×K	314.15	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	163.42	J/mol×K	316.65	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	164.11	J/mol×K	319.15	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	164.82	J/mol×K	321.65	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	165.00	J/mol×K	324.15	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	165.97	J/mol×K	326.65	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	166.72	J/mol×K	329.15	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	167.29	J/mol×K	331.65	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	167.78	J/mol×K	334.15	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	168.53	J/mol×K	336.65	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	169.12	J/mol×K	339.15	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	170.01	J/mol×K	341.65	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	170.43	J/mol×K	344.15	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	170.49	J/mol×K	346.65	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	171.50	J/mol×K	349.15	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	173.02	J/mol×K	351.65	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	173.09	J/mol×K	353.15	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
η	[0.0003540; 0.0004993]	Pa×s	[283.15; 318.15]
η	0.0004993	Pa×s	283.15	Experimental and Predicted Viscosities of Binary Mixtures Containing Chlorinated and Oxygenated Compounds
η	0.0004993	Pa×s	283.15	Viscosities of Binary Mixtures Containing Isomeric Chlorobutanes and Diisopropylether: Experimental and Predicted Values
η	0.0004701	Pa×s	288.15	Viscosities of Binary Mixtures Containing Isomeric Chlorobutanes and Diisopropylether: Experimental and Predicted Values
η	0.0004770	Pa×s	288.15	Densities and Viscosities of Binary Mixtures of 1-Chlorobutane with Butanol Isomers at Several Temperatures
η	0.0004701	Pa×s	288.15	Experimental and Predicted Viscosities of Binary Mixtures Containing Chlorinated and Oxygenated Compounds
η	0.0004433	Pa×s	293.15	Viscosities of Binary Mixtures Containing Isomeric Chlorobutanes and Diisopropylether: Experimental and Predicted Values
η	0.0004433	Pa×s	293.15	Experimental and Predicted Viscosities of Binary Mixtures Containing Chlorinated and Oxygenated Compounds
η	0.0004214	Pa×s	298.15	Viscosities of Binary Mixtures Containing Isomeric Chlorobutanes and Diisopropylether: Experimental and Predicted Values
η	0.0004212	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	0.0004214	Pa×s	298.15	Experimental and Predicted Viscosities of Binary Mixtures Containing Chlorinated and Oxygenated Compounds
η	0.0004290	Pa×s	298.15	Densities and Viscosities of Binary Mixtures of 1-Chlorobutane with Butanol Isomers at Several Temperatures
η	0.0004273	Pa×s	298.15	Measurements, Correlations, and Predictions of Viscosities for the Ternary Mixture (2-Butanol + Hexane + 1-Chlorobutane) at 298.15 K and 313.15 K
η	0.0004090	Pa×s	303.15	Densities and Viscosities of Binary Mixtures of 1-Chlorobutane with Butanol Isomers at Several Temperatures
η	0.0004050	Pa×s	303.15	Experimental and Predicted Viscosities of Binary Mixtures Containing Chlorinated and Oxygenated Compounds
η	0.0004050	Pa×s	303.15	Viscosities of Binary Mixtures Containing Isomeric Chlorobutanes and Diisopropylether: Experimental and Predicted Values
η	0.0003885	Pa×s	308.15	Experimental and Predicted Viscosities of Binary Mixtures Containing Chlorinated and Oxygenated Compounds
η	0.0003900	Pa×s	308.15	Densities and Viscosities of Binary Mixtures of 1-Chlorobutane with Butanol Isomers at Several Temperatures
η	0.0003885	Pa×s	308.15	Viscosities of Binary Mixtures Containing Isomeric Chlorobutanes and Diisopropylether: Experimental and Predicted Values
η	0.0003645	Pa×s	313.15	Measurements, Correlations, and Predictions of Viscosities for the Ternary Mixture (2-Butanol + Hexane + 1-Chlorobutane) at 298.15 K and 313.15 K
η	0.0003642	Pa×s	313.15	Experimental and Predicted Viscosities of Binary Mixtures Containing Chlorinated and Oxygenated Compounds
η	0.0003642	Pa×s	313.15	Viscosities of Binary Mixtures Containing Isomeric Chlorobutanes and Diisopropylether: Experimental and Predicted Values
η	0.0003720	Pa×s	313.15	Densities and Viscosities of Binary Mixtures of 1-Chlorobutane with Butanol Isomers at Several Temperatures
η	0.0003640	Pa×s	313.15	Densities and Viscosities of the Binary Mixtures of Tetrahydrofuran with Isomeric Chlorobutanes at 298.15 K and 313.15 K
η	0.0003540	Pa×s	318.15	Densities and Viscosities of Binary Mixtures of 1-Chlorobutane with Butanol Isomers at Several Temperatures
ΔvapH	[29.40; 37.20]	kJ/mol	[304.00; 358.00]
ΔvapH	35.60	kJ/mol	304.00	NIST
ΔvapH	32.70 ± 0.10	kJ/mol	313.00	NIST
ΔvapH	37.20	kJ/mol	318.00	NIST
ΔvapH	35.00	kJ/mol	323.00	NIST
ΔvapH	31.80 ± 0.10	kJ/mol	328.00	NIST
ΔvapH	30.90 ± 0.10	kJ/mol	343.00	NIST
ΔvapH	30.90	kJ/mol	349.50	NIST
ΔvapH	30.00	kJ/mol	351.60	KDB
ΔvapH	30.39	kJ/mol	351.70	NIST
ΔvapH	30.00 ± 0.10	kJ/mol	358.00	NIST
ΔvapH	29.40 ± 0.10	kJ/mol	358.00	NIST
ν	[0.0000004; 0.0000006]	m2/s	[283.15; 313.15]
ν	0.0000006	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	[4.98; 101.40]	kPa	[278.15; 351.61]
Pvap	4.98	kPa	278.15	Isothermal (vapour + liquid) equilibrium at several temperatures of (1-chlorobutane + 1-octanol, or 1-decanol)
Pvap	6.51	kPa	283.15	Isothermal (vapour + liquid) equilibrium at several temperatures of (1-chlorobutane + 1-octanol, or 1-decanol)
Pvap	8.40	kPa	288.15	Experimental and predicted vapour-liquid equilibrium of the binary mixtures n-heptane + chlorobutane isomers
Pvap	8.40	kPa	288.15	Isothermal vapour-liquid equilibria and excess enthalpies for the binary mixtures containing an isomeric chlorobutane and diisopropyl ether
Pvap	8.40	kPa	288.15	Experimental and predicted properties of the binary mixtures containing an isomeric chlorobutane and butyl ethyl ether
Pvap	8.38	kPa	288.15	Isothermal (vapour + liquid) equilibrium at several temperatures of (1-chlorobutane + 1-octanol, or 1-decanol)
Pvap	10.69	kPa	293.15	Isothermal (vapour + liquid) equilibrium at several temperatures of (1-chlorobutane + 1-octanol, or 1-decanol)
Pvap	13.72	kPa	298.15	(Vapour + liquid) equilibria and excess Gibbs free energies of (cyclohexanone + 1- chlorobutane and + 1,1,1-trichloroethane) binary mixtures at temperatures from (298.15 to 318.15) K
Pvap	13.52	kPa	298.15	Isothermal vapour-liquid equilibria and excess enthalpies for the binary mixtures containing an isomeric chlorobutane and diisopropyl ether
Pvap	13.52	kPa	298.15	Experimental and predicted vapour-liquid equilibrium of the binary mixtures n-heptane + chlorobutane isomers
Pvap	13.52	kPa	298.15	Experimental and predicted properties of the binary mixtures containing an isomeric chlorobutane and butyl ethyl ether
Pvap	13.52	kPa	298.15	(Vapour + liquid) equilibrium and excess Gibbs functions of ternary mixtures containing 1-butanol or 2-butanol, n-hexane, and 1-chlorobutane at T = 298.15 K
Pvap	13.50	kPa	298.15	Isothermal (vapour + liquid) equilibrium at several temperatures of (1-chlorobutane + 1-octanol, or 1-decanol)
Pvap	16.97	kPa	303.15	Isothermal (vapour + liquid) equilibrium at several temperatures of (1-chlorobutane + 1-octanol, or 1-decanol)
Pvap	20.66	kPa	308.15	(Vapour + liquid) equilibria and excess Gibbs free energies of (cyclohexanone + 1- chlorobutane and + 1,1,1-trichloroethane) binary mixtures at temperatures from (298.15 to 318.15) K
Pvap	21.05	kPa	308.15	Isothermal (vapour + liquid) equilibrium at several temperatures of (1-chlorobutane + 1-octanol, or 1-decanol)
Pvap	21.04	kPa	308.15	Isothermal vapour-liquid equilibria and excess enthalpies for the binary mixtures containing an isomeric chlorobutane and diisopropyl ether
Pvap	21.04	kPa	308.15	Experimental and predicted properties of the binary mixtures containing an isomeric chlorobutane and butyl ethyl ether
Pvap	21.04	kPa	308.15	Experimental and predicted vapour-liquid equilibrium of the binary mixtures n-heptane + chlorobutane isomers
Pvap	25.72	kPa	313.15	Excess enthalpies and isothermal (vapour + liquid) equilibria of (1-methyl-2-pyrrolidone + 1-chloroalkane or +,?-dichloroalkane) mixtures
Pvap	25.72	kPa	313.15	(Vapour + liquid) equilibria and excess molar enthalpies for binary mixtures containing N,N-dialkylamides and 1-chloroalkanes
Pvap	25.88	kPa	313.15	Isothermal (vapour + liquid) equilibrium at several temperatures of (1-chlorobutane + 1-octanol, or 1-decanol)
Pvap	31.59	kPa	318.15	Isothermal (vapour + liquid) equilibrium at several temperatures of (1-chlorobutane + 1-octanol, or 1-decanol)
Pvap	31.46	kPa	318.15	(Vapour + liquid) equilibria and excess Gibbs free energies of (cyclohexanone + 1- chlorobutane and + 1,1,1-trichloroethane) binary mixtures at temperatures from (298.15 to 318.15) K
Pvap	38.26	kPa	323.15	Isothermal (vapour + liquid) equilibrium at several temperatures of (1-chlorobutane + 1-octanol, or 1-decanol)
Pvap	40.87	kPa	325.00	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	44.16	kPa	327.14	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	46.87	kPa	328.66	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	48.37	kPa	329.60	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	48.83	kPa	329.78	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	51.33	kPa	331.28	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	332.28	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	54.07	kPa	332.68	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	59.61	kPa	335.44	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	65.42	kPa	338.11	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	72.23	kPa	341.04	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	344.14	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	87.52	kPa	346.84	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	92.35	kPa	348.63	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	351.53	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	101.40	kPa	351.61	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	[1.39131; 1.40750]		[283.15; 313.15]
n0	1.40750		283.15	Volumetric, Acoustic, and Refractive Properties of Isomeric Chlorobutanes with Diisopropyl Ether
n0	1.40450		288.15	Excess Molar Volumes, Viscosities, and Refractive Indexes for Binary Mixtures of 1-Chlorobutane with Four Alcohols at T = (288.15, 298.15 and 308.15) K
n0	1.40481		288.15	Volumetric, Acoustic, and Refractive Properties of Isomeric Chlorobutanes with Diisopropyl Ether
n0	1.40212		293.15	Volumetric, Acoustic, and Refractive Properties of Isomeric Chlorobutanes with Diisopropyl Ether
n0	1.39910		298.15	Isothermal (vapour + liquid) equilibria and excess Gibbs free energies in some binary (cyclopentanone + chloroalkane) mixtures at temperatures from 298.15 K to 318.15 K
n0	1.39960		298.15	Densities, Excess Molar Volumes, Viscosities, and Refractive Indices of Binary Mixtures of n-Butyl Acetate with 1-Chloroalkanes (C4 C8) at 298.15 K
n0	1.39930		298.15	Excess Molar Volumes, Viscosities, and Refractive Indexes for Binary Mixtures of 1-Chlorobutane with Four Alcohols at T = (288.15, 298.15 and 308.15) K
n0	1.39950		298.15	Volumetric and refractive properties of binary mixtures containing 1,4-dioxane and chloroalkanes
n0	1.39953		298.15	Isothermal vapor liquid equilibria and excess Gibbs free energies in some binary nitroalkane + chloroalkane mixtures at temperatures from 298.15 K to 318.15 K
n0	1.39950		298.15	Volumetric, Acoustic, and Refractive Properties of Isomeric Chlorobutanes with Diisopropyl Ether
n0	1.39953		298.15	Isothermal Vapor-Liquid Equilibrium of Binary Mixtures Containing 1-Chlorobutane, Ethanol, or Acetonitrile
n0	1.39672		303.15	Volumetric, Acoustic, and Refractive Properties of Isomeric Chlorobutanes with Diisopropyl Ether
n0	1.39410		308.15	Excess Molar Volumes, Viscosities, and Refractive Indexes for Binary Mixtures of 1-Chlorobutane with Four Alcohols at T = (288.15, 298.15 and 308.15) K
n0	1.39395		308.15	Volumetric, Acoustic, and Refractive Properties of Isomeric Chlorobutanes with Diisopropyl Ether
n0	1.39133		313.15	Volumetric and refractive properties of binary mixtures containing 1,4-dioxane and chloroalkanes
n0	1.39131		313.15	Volumetric, Acoustic, and Refractive Properties of Isomeric Chlorobutanes with Diisopropyl Ether
ρl	[835.30; 925.80]	kg/m3	[253.15; 338.15]
ρl	925.80	kg/m3	253.15	Density of Some 1-Chloroalkanes within the Temperature Range from (253.15 to 423.15) K
ρl	917.40	kg/m3	263.15	Density of Some 1-Chloroalkanes within the Temperature Range from (253.15 to 423.15) K
ρl	907.30	kg/m3	273.15	Density of Some 1-Chloroalkanes within the Temperature Range from (253.15 to 423.15) K
ρl	896.60	kg/m3	283.15	Density of Some 1-Chloroalkanes within the Temperature Range from (253.15 to 423.15) K
ρl	892.18	kg/m3	288.15	Densities and Excess Molar Volumes of the Binary Mixtures of Cyclopentanone with Chloroalkanes at T = (288.15, 298.15, 308.15, and 318.15) K
ρl	892.10	kg/m3	288.15	Densities and Excess Molar Volumes of the Binary Mixtures of Cyclohexanone with Chloroalkanes at Temperatures between (288.15 and 318.15) K
ρl	891.75	kg/m3	288.15	Excess molar volumes of (1-chlorobutane +heptane + 2-butanone or 2-pentanone) at 288.15 , 303.15 and 313.15 K . Measurements and correlations.
ρl	886.00	kg/m3	293.00	KDB
ρl	885.90	kg/m3	293.15	Density of Some 1-Chloroalkanes within the Temperature Range from (253.15 to 423.15) K
ρl	880.69	kg/m3	298.15	Surface Tensions of the Ternary Mixtures Containing an Isomeric Butanol + n-Hexane + 1-Chlorobutane at 298.15 K
ρl	880.40	kg/m3	298.15	Density of Some 1-Chloroalkanes within the Temperature Range from (253.15 to 423.15) K
ρl	881.05	kg/m3	298.15	Densities and Excess Molar Volumes of the Binary Mixtures of Cyclohexanone with Chloroalkanes at Temperatures between (288.15 and 318.15) K
ρl	881.17	kg/m3	298.15	Volumetric Study for the Binary Nitromethane with Chloroalkane Mixtures at Temperatures in the Range (298.15 to 318.15) K
ρl	880.69	kg/m3	298.15	Surface Tension of Mixtures of Tetrahydrofuran or Tetrahydropyran with Isomeric Chlorobutanes
ρl	880.69	kg/m3	298.15	Thermodynamic study of 2-methyl-tetrahydrofuran with isomeric chlorobutanes
ρl	880.86	kg/m3	298.15	Volumetric properties for binary and ternary systems consist of 1-chlorobutane, n-butylamine and isobutanol at 298.15 K with application of the Prigogine-Flory-Patterson theory and ERAS-Model
ρl	880.69	kg/m3	298.15	Densities and Viscosities of the Ternary Mixtures 2-Methyl-1-propanol (or 2-Methyl-2-propanol) + N-Hexane + 1-Chlorobutane at 298.15 K
ρl	880.69	kg/m3	298.15	Surface study of mixtures containing cyclic ethers and isomeric chlorobutanes
ρl	881.12	kg/m3	298.15	Densities and Excess Molar Volumes of the Binary Mixtures of Cyclopentanone with Chloroalkanes at T = (288.15, 298.15, 308.15, and 318.15) K
ρl	874.90	kg/m3	303.15	Density of Some 1-Chloroalkanes within the Temperature Range from (253.15 to 423.15) K
ρl	875.10	kg/m3	303.15	Excess molar volumes of (1-chlorobutane +heptane + 2-butanone or 2-pentanone) at 288.15 , 303.15 and 313.15 K . Measurements and correlations.
ρl	869.93	kg/m3	308.15	Densities and Excess Molar Volumes of the Binary Mixtures of Cyclopentanone with Chloroalkanes at T = (288.15, 298.15, 308.15, and 318.15) K
ρl	869.86	kg/m3	308.15	Densities and Excess Molar Volumes of the Binary Mixtures of Cyclohexanone with Chloroalkanes at Temperatures between (288.15 and 318.15) K
ρl	870.00	kg/m3	308.15	Volumetric Study for the Binary Nitromethane with Chloroalkane Mixtures at Temperatures in the Range (298.15 to 318.15) K
ρl	863.83	kg/m3	313.15	Excess molar volumes of (1-chlorobutane +heptane + 2-butanone or 2-pentanone) at 288.15 , 303.15 and 313.15 K . Measurements and correlations.
ρl	863.90	kg/m3	313.15	Density of Some 1-Chloroalkanes within the Temperature Range from (253.15 to 423.15) K
ρl	858.52	kg/m3	318.15	Densities and Excess Molar Volumes of the Binary Mixtures of Cyclohexanone with Chloroalkanes at Temperatures between (288.15 and 318.15) K
ρl	858.67	kg/m3	318.15	Volumetric Study for the Binary Nitromethane with Chloroalkane Mixtures at Temperatures in the Range (298.15 to 318.15) K
ρl	858.58	kg/m3	318.15	Densities and Excess Molar Volumes of the Binary Mixtures of Cyclopentanone with Chloroalkanes at T = (288.15, 298.15, 308.15, and 318.15) K
ρl	852.10	kg/m3	323.15	Density of Some 1-Chloroalkanes within the Temperature Range from (253.15 to 423.15) K
ρl	835.30	kg/m3	338.15	Density of Some 1-Chloroalkanes within the Temperature Range from (253.15 to 423.15) K
csound,fluid	[1037.26; 1119.00]	m/s	[298.15; 318.15]
csound,fluid	1119.00	m/s	298.15	Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
csound,fluid	1078.01	m/s	308.15	Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
csound,fluid	1037.26	m/s	318.15	Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
γ	[0.02; 0.02]	N/m	[283.15; 313.15]
γ	0.02	N/m	283.15	Surface and bulk behaviour of some (n-hexane + chloroalkane) mixtures
γ	0.02	N/m	288.15	Surface and bulk behaviour of some (n-hexane + chloroalkane) mixtures
γ	0.02	N/m	293.15	Surface and bulk behaviour of some (n-hexane + chloroalkane) mixtures
γ	0.02	N/m	293.20	KDB
γ	0.02	N/m	298.15	Surface and bulk behaviour of some (n-hexane + chloroalkane) mixtures
γ	0.02	N/m	303.15	Surface and bulk behaviour of some (n-hexane + chloroalkane) mixtures
γ	0.02	N/m	308.15	Surface and bulk behaviour of some (n-hexane + chloroalkane) mixtures
γ	0.02	N/m	313.15	Surface and bulk behaviour of some (n-hexane + chloroalkane) mixtures

Datasets

Mass density, kg/m3

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
100.00	283.15	897.36
100.00	288.15	892.04
100.00	293.15	886.36
100.00	298.15	880.82
100.00	303.15	875.21
100.00	308.15	869.76
100.00	313.15	863.9
100.00	318.15	858.39
100.00	323.15	852.47
100.00	328.15	846.87
2000.00	283.15	899.21
2000.00	288.15	893.99
2000.00	293.15	888.35
2000.00	298.15	882.9
2000.00	303.15	877.35
2000.00	308.15	871.94
2000.00	313.15	866.24
2000.00	318.15	860.79
2000.00	323.15	854.85
2000.00	328.15	849.38
5000.00	283.15	902.05
5000.00	288.15	896.87
5000.00	293.15	891.37
5000.00	298.15	886.01
5000.00	303.15	880.6
5000.00	308.15	875.3
5000.00	313.15	869.77
5000.00	318.15	864.38
5000.00	323.15	858.68
5000.00	328.15	853.41
7000.00	283.15	903.87
7000.00	288.15	898.76
7000.00	293.15	893.36
7000.00	298.15	888.03
7000.00	303.15	882.68
7000.00	308.15	877.49
7000.00	313.15	871.92
7000.00	318.15	866.7
7000.00	323.15	861.15
7000.00	328.15	855.89
10000.00	283.15	906.6
10000.00	288.15	901.58
10000.00	293.15	896.28
10000.00	298.15	890.99
10000.00	303.15	885.78
10000.00	308.15	880.77
10000.00	313.15	875.27
10000.00	318.15	870.14
10000.00	323.15	864.65
10000.00	328.15	859.47
20000.00	283.15	915.16
20000.00	288.15	910.38
20000.00	293.15	905.24
20000.00	298.15	900.33
20000.00	303.15	895.41
20000.00	308.15	890.56
20000.00	313.15	885.35
20000.00	318.15	880.62
20000.00	323.15	875.43
20000.00	328.15	870.67
30000.00	283.15	923.05
30000.00	288.15	918.48
30000.00	293.15	913.5
30000.00	298.15	908.81
30000.00	303.15	904.1
30000.00	308.15	899.63
30000.00	313.15	894.59
30000.00	318.15	890.1
30000.00	323.15	885.16
30000.00	328.15	880.58
40000.00	283.15	930.41
40000.00	288.15	925.97
40000.00	293.15	921.24
40000.00	298.15	916.74
40000.00	303.15	912.24
40000.00	308.15	907.72
40000.00	313.15	903.08
40000.00	318.15	898.75
40000.00	323.15	894.16
40000.00	328.15	889.73
50000.00	283.15	937.2
50000.00	288.15	932.96
50000.00	293.15	928.33
50000.00	298.15	924.0
50000.00	303.15	919.76
50000.00	308.15	915.48
50000.00	313.15	910.86
50000.00	318.15	906.72
50000.00	323.15	902.27
50000.00	328.15	897.97
60000.00	283.15	943.68
60000.00	288.15	939.57
60000.00	293.15	935.0
60000.00	298.15	930.86
60000.00	303.15	926.77
60000.00	308.15	922.6
60000.00	313.15	918.16
60000.00	318.15	914.22
60000.00	323.15	910.0
60000.00	328.15	905.8
65000.00	283.15	946.75
65000.00	288.15	942.66
65000.00	293.15	938.38
65000.00	298.15	934.15
65000.00	303.15	930.08
65000.00	308.15	925.91
65000.00	313.15	921.77
65000.00	318.15	917.73
65000.00	323.15	913.54
65000.00	328.15	909.45
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
288.15	100.00	891.8
288.15	2000.00	893.6
288.15	4100.00	895.6
288.15	6100.00	897.5
288.15	8100.00	899.4
288.15	10100.00	901.3
288.15	12100.00	903.0
288.15	14100.00	904.9
288.15	16300.00	906.7
288.15	18400.00	908.5
288.15	20200.00	910.3
298.15	100.00	880.6
298.15	2000.00	882.6
298.15	4100.00	884.9
298.15	6100.00	886.8
298.15	8100.00	888.7
298.15	10100.00	890.9
298.15	12100.00	892.8
298.15	14200.00	894.7
298.15	16200.00	896.5
298.15	18300.00	898.5
298.15	20400.00	900.2
308.15	100.00	870.0
308.15	2000.00	872.1
308.15	4100.00	874.4
308.15	6100.00	876.5
308.15	8100.00	878.6
308.15	10100.00	880.8
308.15	12100.00	882.9
308.15	14200.00	884.9
308.15	16200.00	886.8
308.15	18300.00	888.8
308.15	20200.00	890.6
318.15	100.00	859.1
318.15	2000.00	861.5
318.15	4000.00	863.8
318.15	6100.00	866.3
318.15	8100.00	868.7
318.15	10100.00	870.9
318.15	12100.00	873.1
318.15	14100.00	875.1
318.15	16200.00	877.2
318.15	18400.00	879.3
318.15	20200.00	881.2
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	880.6
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.15	100.00	897.21
283.15	2500.00	899.51
283.15	5000.00	901.82
283.15	10000.00	906.3
283.15	15000.00	910.57
283.15	20000.00	914.69
283.15	25000.00	918.63
283.15	30000.00	922.33
283.15	35000.00	926.05
293.15	100.00	886.18
293.15	2500.00	888.63
293.15	5000.00	891.13
293.15	10000.00	895.89
293.15	20000.00	904.73
293.15	25000.00	908.9
293.15	30000.00	912.88
293.15	35000.00	916.77
298.15	100.00	880.63
298.15	2500.00	883.17
298.15	5000.00	885.72
298.15	10000.00	890.65
298.15	15000.00	895.36
298.15	20000.00	899.79
298.15	25000.00	904.09
298.15	30000.00	908.22
298.15	35000.00	912.17
303.15	100.00	874.92
303.15	2500.00	877.59
303.15	5000.00	880.23
303.15	10000.00	885.43
303.15	15000.00	890.24
303.15	20000.00	894.84
303.15	25000.00	899.24
303.15	30000.00	903.46
303.15	35000.00	907.47
313.15	100.00	863.82
313.15	2500.00	866.65
313.15	5000.00	869.49
313.15	10000.00	874.93
313.15	15000.00	880.07
313.15	20000.00	884.94
313.15	25000.00	889.61
313.15	30000.00	894.04
313.15	35000.00	898.33
323.15	100.00	852.43
323.15	2500.00	855.47
323.15	5000.00	858.54
323.15	10000.00	864.35
323.15	15000.00	869.85
323.15	20000.00	875.03
323.15	25000.00	879.94
323.15	30000.00	884.62
323.15	35000.00	889.1
333.15	100.00	840.79
333.15	2500.00	844.06
333.15	5000.00	847.37
333.15	10000.00	853.61
333.15	15000.00	859.47
333.15	20000.00	864.97
333.15	25000.00	870.17
333.15	30000.00	875.12
333.15	35000.00	879.82
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	13.52	880.805
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[103.74; 233.96]	J/mol×K	[273.00; 1000.00]	Joback Predicted correlation
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K
Coefficient A			1.21430e+01
Coefficient B			3.90620e-01
Coefficient C			-2.14200e-04
Coefficient D			4.54000e-08
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	103.74	J/mol×K	273.00	Calculated Property
Cp,gas	125.54	J/mol×K	353.78	Calculated Property
Cp,gas	145.17	J/mol×K	434.56	Calculated Property
Cp,gas	162.77	J/mol×K	515.33	Calculated Property
Cp,gas	178.50	J/mol×K	596.11	Calculated Property
Cp,gas	192.49	J/mol×K	676.89	Calculated Property
Cp,gas	204.89	J/mol×K	757.67	Calculated Property
Cp,gas	215.84	J/mol×K	838.44	Calculated Property
Cp,gas	225.48	J/mol×K	919.22	Calculated Property
Cp,gas	233.96	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.66]	kPa	[255.28; 373.41]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.45467e+01
Coefficient B			-3.09635e+03
Coefficient C			-3.81330e+01
Temperature range, min.			255.28
Temperature range, max.			373.41
Pvap	1.33	kPa	255.28	Calculated Property
Pvap	3.01	kPa	268.41	Calculated Property
Pvap	6.21	kPa	281.53	Calculated Property
Pvap	11.90	kPa	294.66	Calculated Property
Pvap	21.41	kPa	307.78	Calculated Property
Pvap	36.48	kPa	320.91	Calculated Property
Pvap	59.30	kPa	334.03	Calculated Property
Pvap	92.48	kPa	347.16	Calculated Property
Pvap	139.11	kPa	360.28	Calculated Property
Pvap	202.66	kPa	373.41	Calculated Property
Pvap	[2.33e-06; 3601.12]	kPa	[150.05; 537.00]	KDB Vapor Pressure Data
Equation			ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K
Coefficient A			7.92413e+01
Coefficient B			-6.56700e+03
Coefficient C			-9.70121e+00
Coefficient D			7.48517e-06
Coefficient E			0.00000e+00
Temperature range, min.			150.05
Temperature range, max.			537.00
Pvap	2.33e-06	kPa	150.05	Calculated Property
Pvap	3.87e-03	kPa	193.04	Calculated Property
Pvap	0.31	kPa	236.04	Calculated Property
Pvap	5.25	kPa	279.03	Calculated Property
Pvap	36.74	kPa	322.03	Calculated Property
Pvap	150.09	kPa	365.02	Calculated Property
Pvap	435.10	kPa	408.02	Calculated Property
Pvap	1006.70	kPa	451.01	Calculated Property
Pvap	2003.11	kPa	494.01	Calculated Property
Pvap	3601.12	kPa	537.00	Calculated Property
Pvap	[1.34; 102.46]	kPa	[256.40; 351.70]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.38060e+01
Coefficient B			-2.72373e+03
Coefficient C			-5.48850e+01
Reference			Kemme and Kreps, 1969
Temperature range, min.			256.40
Temperature range, max.			351.70
Pvap	1.34	kPa	256.40	Calculated Property
Pvap	2.62	kPa	266.99	Calculated Property
Pvap	4.83	kPa	277.58	Calculated Property
Pvap	8.42	kPa	288.17	Calculated Property
Pvap	13.97	kPa	298.76	Calculated Property
Pvap	22.24	kPa	309.34	Calculated Property
Pvap	34.11	kPa	319.93	Calculated Property
Pvap	50.62	kPa	330.52	Calculated Property
Pvap	72.97	kPa	341.11	Calculated Property
Pvap	102.46	kPa	351.70	Calculated Property

Similar Compounds

Find more compounds similar to Butane, 1-chloro-.

Mixtures

• n-Hexane + Butane, 1-chloro-
• 1-Propanol + Butane, 1-chloro-
• 1,3-Dioxolane + Butane, 1-chloro-
• Butane, 1-chloro- + 1,4-Dioxane
• Butane, 1-chloro- + Methane, nitro-
• Tetrahydropyran + Butane, 1-chloro-
• Butane, 1-chloro- + 1-Octanol
• Butane, 1-chloro- + 1-Decanol
• Butane, 1-chloro- + Cyclopentanone
• Pyridine + Butane, 1-chloro-
• 2-Pyrrolidinone, 1-methyl- + Butane, 1-chloro-
• n-Hexane + 1-Butanol + Butane, 1-chloro-
• Butane, 1-chloro- + Water
• 1H-Imidazole, 1-methyl- + Butane, 1-chloro- + Water
• sodium chloride + Butane, 1-chloro- + Water
• Butane, 1-chloro- + Ethane, nitro-
• Butane, 1-chloro- + Heptane
• Acetic acid, pentyl ester + Butane, 1-chloro-
• Butane, 1-chloro- + Cyclohexane
• Toluene + Butane, 1-chloro-

Find more mixtures with Butane, 1-chloro-.

Sources

• KDB Vapor Pressure Data
• 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
• Densities, Excess Molar Volumes, Viscosities, and Refractive Indices of Binary Mixtures of n-Butyl Acetate with 1-Chloroalkanes (C4 C8) at 298.15 K
• 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
• Solubility of chlorobutane, ethyl methacrylate and trifluoroethyl acrylate in supercritical carbon dioxide
• Excess molar volume and viscosity study for the ternary system tetrahydrofuran (1) + 1-chlorobutane (2) + 2-butanol (3) at 283.15, 298.15 and 313.15 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
• Measurement and prediction of multicomponent diffusion coefficients in four ternary liquid systems
• Limiting activity coefficients of 1-chlorobutane in water and in aqueous solutions of substances involved in synthesis of ionic liquids
• Isothermal vapour-liquid equilibria and excess enthalpies for the binary mixtures containing an isomeric chlorobutane and diisopropyl ether
• Isothermal vapor liquid equilibria and excess Gibbs free energies in some binary nitroalkane + chloroalkane mixtures at temperatures from 298.15 K to 318.15 K
• Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
• Experimental and predicted vapour-liquid equilibrium of the binary mixtures n-heptane + chlorobutane isomers
• Abraham model linear free energy relationships for describing the partitioning and solubility behavior of nonelectrolyte organic solutes dissolved in pyridine at 298.15 K
• Isothermal (vapour + liquid) equilibrium at several temperatures of (1-chlorobutane + 1-octanol, or 1-decanol)
• Volumetric and refractive properties of binary mixtures containing 1,4-dioxane and chloroalkanes
• Surface study of mixtures containing cyclic ethers and isomeric chlorobutanes
• (Vapour + liquid) equilibria and excess molar enthalpies for binary mixtures containing N,N-dialkylamides and 1-chloroalkanes
• Isothermal (vapour + liquid) equilibria and excess Gibbs free energies in some binary (cyclopentanone + chloroalkane) mixtures at temperatures from 298.15 K to 318.15 K
• Excess enthalpies and isothermal (vapour + liquid) equilibria of (1-methyl-2-pyrrolidone + 1-chloroalkane or +,?-dichloroalkane) mixtures
• Surface and bulk behaviour of some (n-hexane + chloroalkane) mixtures
• (Vapour + liquid) equilibrium and excess Gibbs functions of ternary mixtures containing 1-butanol or 2-butanol, n-hexane, and 1-chlorobutane at T = 298.15 K
• (Vapour + liquid) equilibria and excess Gibbs free energies of (cyclohexanone + 1- chlorobutane and + 1,1,1-trichloroethane) binary mixtures at temperatures from (298.15 to 318.15) K
• Volumetric and acoustic behaviour of systems containing n-hexane, or n-heptane and isomeric chlorobutanes
• Experimental and predicted properties of the binary mixtures containing an isomeric chlorobutane and butyl ethyl ether
• Refractive indices and static permittivities of systems containing n-hexane or n-heptane and isomeric chlorobutanes
• Abraham model correlations for describing the thermodynamic properties of solute transfer into pentyl acetate based on headspace chromatographic and solubility measurements
• Improving the method of solution calorimetry for evaluation of the enthalpies of phase transitions and condensed state enthalpies of formation
• Thermodynamic study of 2-methyl-tetrahydrofuran with isomeric chlorobutanes
• Volumetric properties for binary and ternary systems consist of 1-chlorobutane, n-butylamine and isobutanol at 298.15 K with application of the Prigogine-Flory-Patterson theory and ERAS-Model
• Excess molar volumes of (1-chlorobutane +heptane + 2-butanone or 2-pentanone) at 288.15 , 303.15 and 313.15 K . Measurements and correlations.
• Examination of hydrogen-bonding interactions between dissolved solutes and alkylbenzene solvents based on Abraham model correlations derived from measured enthalpies of solvation
• Excess properties from p.rho.T data for n-heptane + isomeric chlorobutane mixtures
• Effect of halogen substitution on the enthalpies of solvation and hydrogen bonding of organic solutes in chlorobenzene and 1,2-dichlorobenzene derived using multi-parameter correlations
• 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
• Measurements, Correlations, and Predictions of Viscosities for the Ternary Mixture (2-Butanol + Hexane + 1-Chlorobutane) at 298.15 K and 313.15 K
• 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
• Solubilities of Some Long-Chain n-Alkanes in Dipropyl Ether, Dibutyl Ether, 1-Chlorobutane, and 1-Chlorooctane as Functions of Temperature
• Excess Molar Volumes, Viscosities, and Refractive Indexes for Binary Mixtures of 1-Chlorobutane with Four Alcohols at T = (288.15, 298.15 and 308.15) K
• Densities and Viscosities of Binary Mixtures of 1-Chlorobutane with Butanol Isomers at Several Temperatures
• Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
• Solubility of Imidazoles, Benzimidazoles, and Phenylimidazoles in Dichloromethane, 1-Chlorobutane, Toluene, and 2-Nitrotoluene
• Densities and Viscosities of the Binary Mixtures of Tetrahydrofuran with Isomeric Chlorobutanes at 298.15 K and 313.15 K
• Surface Tensions of the Ternary Mixtures Containing an Isomeric Butanol + n-Hexane + 1-Chlorobutane at 298.15 K
• Activity Coefficients at Infinite Dilution for Hydrocarbons in Fatty Alcohols Determined by Gas-Liquid Chromatography
• Volumetric, Acoustic, and Refractive Properties of Isomeric Chlorobutanes with Diisopropyl Ether
• Experimental and Predicted Kinematic Viscosities for Alkane + Chloroalkane Mixtures
• Activity Coefficients at Infinite Dilution by GLC in Alkanediamines as Stationary Phases
• Volumetric Properties of Short-Chain Chloroalkanes
• Volumetric Study for the Binary Nitromethane with Chloroalkane Mixtures at Temperatures in the Range (298.15 to 318.15) K
• Densities and Isothermal Compressibilities at Pressures up to 20 MPa of the Systems N,N-Dimethylformamide or N,N-Dimethylacetamide + 1-Chloroalkane
• Density of Some 1-Chloroalkanes within the Temperature Range from (253.15 to 423.15) K
• Densities and Isothermal Compressibilities at Pressures up to 20 MPa of the Systems 1-Methyl-2-pyrrolidone + 1-Chloroalkane or + r,u-Dichloroalkane
• Densities and Excess Volumes of the 1-Chlorobutane + n-Hexane System at Temperatures from (283.15 to 333.15) K and Pressures from (0.1 to 35) MPa
• Densities and Viscosities of the Ternary Mixtures 2-Methyl-1-propanol (or 2-Methyl-2-propanol) + N-Hexane + 1-Chlorobutane at 298.15 K
• Isothermal Vapor-Liquid Equilibrium of Binary Mixtures Containing 1-Chlorobutane, Ethanol, or Acetonitrile
• Phase Behavior, Densities, and Isothermal Compressibility of Carbon Dioxide + 1-Bromobutane, Carbon Dioxide + 1-Chlorobutane, and Carbon Dioxide + 1-Methylimidazole
• Densities and Excess Molar Volumes of the Binary Mixtures of Cyclohexanone with Chloroalkanes at Temperatures between (288.15 and 318.15) 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
• Densities and Excess Molar Volumes of the Binary Mixtures of Cyclopentanone with Chloroalkanes at T = (288.15, 298.15, 308.15, and 318.15) 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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